Breathable composite sheet structure and absorbent articles utilizing same

ABSTRACT

A breathable composite sheet material, a method for making such a sheet material, and an absorbent article utilizing the sheet material are provided. The composite sheet material is comprised of a thermoplastic film adhered directly to a fibrous substrate. The thermoplastic film comprises at least 50% by weight of a polymer material from the group of block copolyether esters, block copolyether amides and polyurethanes. The substrate comprises a fibrous web of at least 50% by weight of polyolefin polymer synthetic fibers. The composite sheet exhibits a peel strength of at least 0.1 N/cm, a dynamic fluid transmission of less than about 0.75 g/m 2  when subjected to an impact energy of about 2400 joules/m 2 , and a moisture vapor transmission rate, according to the desiccant method, of at least 1500 g/m 2 /24 hr. The absorbent article comprises (a) a topsheet; (b) a backsheet; and (c) an absorbent core located between the topsheet and the backsheet; wherein the backsheet comprises the non-porous, substantially fluid impermeable, moisture vapor permeable composite sheet material described above. The composite sheet material is oriented such that the film layer of the composite sheet material faces toward the absorbent core. The absorbent article may comprise a disposable diaper.

CROSS REFERENCE TO RELATED APPLICATIONS

This application is a divisional of 09/194,378, filed Nov. 25, 1998, nowU.S. Pat. No. 6,677,258 which is a 371 of PCT/US97/09215 May 29, 1997.

FIELD OF THE INVENTION

This invention relates to a moisture vapor permeable, substantiallyliquid impermeable composite sheet structure useful in apparel, surgicaldrapes, sterile wraps, packaging materials, protective covers,construction materials, and personal care absorbent articles such asdiapers and sanitary napkins. More particularly, the invention isdirected to a moisture vapor permeable film and fibrous substrate thatcombine to form a composite sheet that is durable, strong, and flexible,that acts as a barrier to liquids, bacteria and odors, yet is alsohighly permeable to moisture vapor. The invention is also directed to anabsorbent article having a backsheet made of the aforementionedcomposite sheet of the invention.

BACKGROUND OF THE INVENTION

Sheet materials used in making medical drapes, medical gowns andabsorbent articles, such as diapers and sanitary napkins, must be bothcomfortable and substantially liquid impermeable. Manufacturing and userequirements for such products often demand that the sheet material alsobe strong and durable.

Infants and other incontinent individuals wear absorbent articles toreceive and contain urine and other body exudates. Absorbent articlesfunction both to contain the discharged materials and to isolate thesematerials from the body of the wearer and from the wearer's garments andbed clothing. Disposable absorbent articles having many different basicdesigns are known to the art. It is also known that the exterior ofabsorbent articles can be covered with a flexible, fluid and vaporimpervious sheet to prevent any absorbed fluid from passing through thearticle and soiling adjacent articles such as clothing, bedding and thelike. These outer covers, generally referred to as backsheets, are oftenconstructed from fluid and vapor impervious films such as polyethylene.

While plastic films do an admirable job of containing liquids, they arenot pleasing to the touch and they do not readily pass moisture vapor,which makes garments made with plastic films uncomfortable andirritating to the skin. Plastic films have been made more acceptable forapparel and personal care applications by creating micropores in thefilms to make breathable microporous films. In microporous films,moisture is transported through the films by way of small gaps or holesin the film. One notable microporous film composite is made frompolytetrafluoroethylene that is adhered to a textile material with anadhesive, as disclosed in British Patent Application No. 2,024,100.Microporous films adhesively bonded to textile substrates have been usedin a variety of apparel products, including absorbent articles, asdisclosed in PCT Patent Publication Nos. WO 95/16562 and WO 96/39031.

Laminates of a microporous film and a fibrous textile substrate have anumber of disadvantages, including that their manufacture requires aseparate adhesive bonding step after the film is made, and that suchlaminates permit some seepage of fluids when used as the backsheet in anabsorbent article. For example, when such microporous film laminates areused as a backsheet of a disposable diaper, the backsheet may permit thetransmission of some urine through the pores in the backsheet when aninfant wearing the diaper sits down. Liquid seepage through microporousfilm laminates is especially likely to occur when the microporouslaminate is exposed to a fluid with a low surface tension, as forexample when urine in a diaper is exposed to surfactants within thediaper itself.

When fluids seep through the pores of a microporous film, bacteria,viruses, and other microbes can pass through the film along with thefluids. Likewise, the passage of fluids through laminates made withmicroporous films, whether the fluids are liquid or gaseous, alsoincreases the odors that emanate from such laminates. Microbialadsorbents have been added to some microporous films in an attempt tocapture microbes passing through such films, as disclosed in PCT PatentPublication No. WO 96/39031. However, it is difficult to distributemicrobial adsorbents throughout a microporous film in a manner that willadsorb all microbes seeping through the holes in the film. Likewise,microbial adsorbents are unlikely to prevent the passage of odorsthrough the pores in a microporous film.

Moisture vapor permeable films comprised of polyether block copolymers,like the film disclosed in U.S. Pat. No. 4,493,870, have an advantage inmedical apparel and personal care applications because such films arenon-porous and therefore substantially impermeable to fluids, but theypermit the passage of moisture vapor. U.S. Pat. No. 4,725,481 suggeststhat such films may be attached to a textile fabric by adhesive bondingor melt bonding. However, the cost of making such films and then bondingthe films to fibrous textile substrates has been high relative tomicroporous film laminates. In addition, known moisture vapor permeablefilms like the films disclosed in U.S. Pat. Nos. 4,725,481 and 5,445,874do not readily adhere to many common nonwoven substrate materials, suchas polyolefin-based nonwoven materials, without the application of aseparate adhesive.

PCT Patent Publication No. WO 95/16746 (assigned to E.I. duPont deNemours & Company (hereinafter “DuPont”)) discloses a composition of apolyether block copolymer combined with a less costly thermoplastichomopolymer so as to make an overall film that is less costly, more heatsealable and more adherable to itself and other substrate materials.However, PCT Patent Publication No. WO 95/16746 does not disclose strongand durable composite sheets of thin breathable films that have beenextruded directly onto fibrous substrates, nor does it disclose a methodfor making such composite sheets.

There is a need for a sheet material that acts as a barrier to fluids,yet is also highly permeable to moisture vapor. There is also a need fora sheet material that readily transmits moisture vapor, butsignificantly deters the passage of bacteria and odors associated withsuch fluids. There is a further need for such a moisture vaporpermeable, fluid impermeable composite sheet material that is alsodurable, strong, and flexible enough to be used in absorbent articles,and can be produced in an economical fashion, i.e., without the use ofadhesives to join the layers of the composite sheet in a separate step.Finally, there is a need for an absorbent article that incorporates sucha moisture vapor permeable composite sheet in the article's backsheet,leg cuffs, waistshields, or other features.

SUMMARY OF THE INVENTION

The invention provides a moisture vapor permeable, substantially liquidimpermeable composite sheet material comprising a fibrous substrate anda moisture vapor permeable thermoplastic film layer. The fibroussubstrate is comprised of at least 50% by weight polyolefin polymerfibers. The moisture vapor permeable thermoplastic film layer is meltbonded directly to one side of said fibrous substrate. The compositesheet exhibits a peel strength of at least 0.1 N/cm, a dynamic fluidtransmission of less than about 0.75 g/m² when subjected to an impactenergy of about 2400 joules/m², and a moisture vapor transmission rate,according to the desiccant method, of at least 1500 g/m²/24 hr.

Preferably the film layer of the composite sheet has an averagethickness of less than 50 microns and is comprised of at least 50% byweight of polymer selected from the group of block copolyether esters,block copolyether amides, polyurethanes, and combinations thereof. It isfurther preferred that the film layer be melt bonded to the substrate inthe absence of an adhesive between the film layer and the substrate. Themore preferred composite sheet has a peel strength of at least 0.15N/cm, a film thickness of less than 30 microns, and a moisture vaportransmission rate, according to the dessicant method, of at least 2500g/m²/24 hr, and a dynamic fluid transmission of less than about 0.5 g/m²when subjected to an impact energy of about 2400 joules/m². The sheet isalso substantially free of micropores such that substantially no liquidmoisture passes through the sheet when tested according to the liquidmoisture seepage test, and the sheet acts as a barrier to the passage ofmicrobes when tested according to the ISO 11607 standard for sterilepackaging materials. The composite sheet should have a machine directiontensile strength and a cross direction tensile strength of at least 1N/cm, and a machine direction elongation and a cross directionelongation of at least 30%.

According to one alternative embodiment of the invention the film layermay be bonded between two fibrous substrates. According to anotheralternative embodiment of the invention, the film layer of the compositesheet may comprise a moisture permeable film having multiple layers,each film layer being comprised of a different moisture vapor permeablethermoplastic polymer composition. One of the multiple layer film layersmay comprise a substantially hydrophilic film layer and one of the filmlayers comprises a substantially hydrophobic film layer. According toyet another embodiment of the invention, the composite sheet may furtherinclude an additional layer of diverse construction and composition fromthe film layer and the fibrous layer, as for example, a microporousfilm.

According to the preferred embodiment of the invention, the film layerof the composite sheet is comprised at least 50% by weight of a FractionA consisting essentially of polymer from the group of block copolyetheresters, block copolyether amides, polyurethanes and combinationsthereof, at least 5% by weight of a Fraction B consisting essentially ofa polymer from the group of homopolymers of an alpha-olefin, copolymersor terpolymers containing an alpha-olefin and one or more othermonomers, and a block copolymer of a vinylarene and a conjugated diene,and at least 0.1% by weight of a Fraction C consisting essentially of acompatibilizer for Fractions A and B. The film Fraction C preferablyconsists essentially of homopolymers, copolymers and terpolymers withbackbones that are compatible with Fraction B, the backbones beinggrafted with a monomer having a functional group that is compatible withFraction A. Film Fraction C is preferably a polymer with a backboneidentical to Fraction B, which backbone is grafted with monomer selectedfrom the group of alpha- and beta-ethylenically unsaturated carbonicacids and anhydrides, and derivatives thereof.

The invention also provides a method for making the breathable compositesheet material described above. Thermoplastic polymer selected from thegroup of block copolyether esters, block copolyether amides,polyurethanes, and combinations thereof is initially mixed. Next, themixture is simultaneously melted and mixed, and is then melt extrudedthrough a flat film die. The molten mixture is coated directly onto amoving fibrous substrate and is then forced into intimate contact withthe fibrous substrate. The molten polymer may be forced into intimatecontact with the substrate by passing the polymer coated substratebetween cooled nip rollers or by passing the substrate over a vacuumsuction inlet. The composite sheet is finally collected on a collectionroll.

Finally, the invention provides an absorbent article comprising (a) atopsheet; (b) a backsheet; and (c) an absorbent core located between thetopsheet and the backsheet; wherein the backsheet comprises thenon-porous, substantially fluid impermeable, moisture vapor permeablecomposite sheet material described above. Preferably, the compositesheet material is oriented such that the film layer of the compositesheet material faces toward said absorbent core. Where the film layer ofthe composite sheet comprises a multiple layer film with a substantiallyhydrophilic elastomer film layer and a substantially hydrophobicelastomer film, the substantially hydrophilic elastomer film ispreferably located between the substantially hydrophobic elastomer filmand the fibrous substrate. Alternatively, the film layer may furthercomprise a third film layer comprising a substantially hydrophobicelastomer film located between the substantially hydrophilic elastomerfilm and the fibrous substrate. The absorbent article may comprise adisposable diaper.

BRIEF DESCRIPTION OF THE DRAWINGS

The accompanying drawings, which are incorporated in and constitute apart of this specification, illustrate the presently preferredembodiments of the invention and, together with the description, serveto explain the principles of the invention.

FIG. 1 is a cross-sectional view of the composite sheet structure of theinvention.

FIG. 2 is a cross-sectional view of a composite sheet structureaccording to an alternative embodiment of the invention.

FIG. 3 is a schematic representation of a process by which the compositesheet structure of the invention is made.

FIG. 4 is a plan view of a disposable diaper embodiment of the presentinvention having portions cut away to reveal underlying structure, asviewed from the inner surface of the diaper.

FIG. 5 is a simplified plan view of the disposable diaper of the presentinvention in its flat uncontracted condition showing the various panelsor zones of the diaper.

FIG. 6 is a plan view of another embodiment of a diaper backsheet of thepresent invention.

FIG. 7 is a simplified illustration of an apparatus used for measuringdynamic fluid transmission of a sheet material.

DETAILED DESCRIPTION OF THE INVENTION

Reference will now be made in detail to the presently preferredembodiments of the invention, examples of which are illustrated below.

The liquid impermeable, moisture vapor permeable composite sheetstructure of the invention is shown in FIG. 1. The composite sheet 10 iscomprised of a fibrous substrate 14 to which a moisture vapor permeableand substantially liquid impermeable film 12 is directly adhered. Suchcomposite sheets are sometimes referred to as laminate structures. Themoisture permeable film is substantially free of pinholes or pores, yetstill has a relatively high rate of moisture vapor transmission. As usedherein, “pinholes” means small holes inadvertently formed in a filmeither during manufacture or processing of the film, while “pores” meanssmall holes in a film that are intentionally formed in the film in orderto make the film porous to air, moisture vapor or liquids. In thepreferred embodiment of the invention, the moisture vapor permeable,substantially liquid impermeable film is a polyether block copolymersuch as copolymers comprised of block copolyether esters, blockcopolyether amides, polyurethanes or combinations thereof. The fibroussubstrate 14 is preferably comprised of synthetic polymer fibers in aform to which the moisture vapor permeable film can be directly adhered.The substrate 14 may be a woven or nonwoven structure, but for costreasons, nonwoven textile structures are preferred for mostapplications. In an alternative embodiment of the invention shown inFIG. 2, the composite sheet structure may be comprised of a moisturepermeable film layer 12 with two fibrous substrates 14 and 16, eachcomprised of synthetic polymer fibers, directly adhered on oppositesides of the film layer.

According to another embodiment of the invention, a thin layer of ablock copolymer selected from a group comprising polyethers, polyamidesand polyurethanes or a combination thereof could be used in conjunctionwith a microporous film to form a laminate film structure. Such astructure should overcome a number of the drawbacks associated withmicroporous films, namely bacteria and liquid seepage and high moistureimpact values, without sacrificing the relatively high MVTR values,often >4,000 g/m²/24 hr, obtainable with some microporous films. Themoisture vapor permeable films of the composite sheet of the presentinvention can be made compatible with polyolefin nonwoven materials andcan also be made compatible with current microporous film compositions,such as those of polyolefinic composition. The moisture vapor permeablefilm layer of the composite sheet of the present invention and amicroporous film can be joined via adhesive lamination or potentially bydirect extrusion coating. The moisture vapor permeable film could becombined with a fibrous substrate in a fashion consistent with thepresent invention. This fibrous substrate and moisture vapor permeablesubstantially liquid impermeable film and microporous film can bejoined, in a fashion consistent with the present invention, with anonwoven sheet bonded to the first side of the moisture vapor permeable,substantially liquid impermeable film layer and with a microporous filmlaminated to the opposing side of the film layer.

Alternatively, the process by which microporosity is incorporated intocurrent polyolefin type microporous films, such as Exxon Exxaire(Catalog No. XBF-100W), could be utilized to impart microporosity to alayer of moisture permeable film in the composite sheet of the presentinvention, e.g., by the incorporation of a material such as calciumcarbonate into the film layer. This would result in a moisture vaporpermeable film layer comprised essentially of polymer from the group ofblock copolyether esters, block copolyether amides, polyurethanes orcombinations thereof, with micropores incorporated therein. This filmlayer could then be formed into a laminate structure with thin layers ofa moisture vapor permeable nonporous film on one or both sides of themicroporous film. Additionally, a fibrous substrate could be bonded tosuch a film laminate structure in a fashion consistent with the presentinvention.

A particularly preferred nonwoven material for the fibrous substrates 14and 16 is a fibrous polyolefin nonwoven web. Suitable polyolefinmaterials include polypropylene and polyethylene spunbonded webs,scrims, woven slit films, carded webs, flashspun webs, and woven ornonwoven sheets comprised of blends of polyolefin fibers or ofpolyolefin fibers and other fibers. Webs of polyolefin fibers can bemade with a variety of desirable properties, including good vaporpermeability, flexibility, softness and strength. Where the compositesheet 10 is to be used in an absorbent article, the substrates 14 and/or16 should preferably have a tensile strength of at least 1 N/cm and anelongation of at least 30% in both the machine and cross directions. Themachine direction is the long direction within the plane of the sheet,i.e., the direction in which the sheet is produced. The cross directionis the direction within the plane of the sheet that is perpendicular tothe machine direction. More preferably, the fibrous substrates have atensile strength of at least 1.5 N/cm and an elongation of at least 50%in both the machine and cross directions. Preferably, the fibroussubstrate also has a porous structure that enhances both moisturepermeability through the composite sheet and physical bonding betweenthe film and substrate layers of the composite sheet.

One polyolefin sheet material that has been advantageously used for thefibrous substrate in the invention is TYPAR® spunbonded polypropylenesheet material. TYPAR® is a registered trademark of DuPont. Anotherfibrous sheet material that has been advantageously used in thecomposite sheet of the invention is a carded, thermally-bondedpolypropylene nonwoven material commercially available from Fiberweb ofSimpsonville, S.C., under the trade designation HEC. Substrates 14 and16 may alternatively be comprised of webs of other synthetic polymermaterials such as polyesters or polyamides, bicomponent fibers made of apolyolefin and one or more other polymers, or blends of polyolefinfibers and fibers comprised of other synthetic materials or othernatural fibers such as cotton or cellulose fibers.

Film layer 12 of the composite sheet structure 10 is a moisture vaporpermeable and substantially liquid impermeable film. The film layer ispreferably extruded directly onto the fibrous substrate 14 and it isthereby adhered to the substrate 14 without the application of anadditional adhesive. Film layer 12 comprises a thermoplastic polymermaterial that can be extruded as a thin, continuous, nonporous,substantially liquid impermeable, moisture vapor permeable film. Layer12 is preferably comprised primarily of a block polyether copolymer,such as a polyether ester copolymer, a polyether amide copolymer, apolyurethane copolymer, or a combination thereof. Preferred copolyetherester block copolymers for film layer 12 are segmented elastomers havingsoft polyether segments and hard polyester segments, as disclosed inU.S. Pat. No. 4,739,012 (assigned to DuPont). Suitable polyether esterblock copolymers are sold by DuPont under the name Hytrel®. Hytrel® is aregistered trademark of DuPont. Suitable copolyether amide copolymersfor film layer 12 are copolyamides available under the name Pebax® fromAtochem Inc. of Glen Rock, N.J., USA. Pebax® is a registered trademarkof Elf Atochem, S.A. of Paris, France. Suitable polyurethanes for use infilm layer 12 are thermoplastic urethanes available under the nameEstane® from The B.F. Goodrich Company of Cleveland, Ohio, USA.

The mixing of the thermoplastic polymer or blends of polymers thatcomprise the film layer of the sheet structure of the invention can beconducted according to methods and techniques known in the art, e.g., byphysical tumble blending followed by extrusion and mixing in a singlescrew extruder equipped with a mixing head such as those available fromDavis-Standard Corp. (Pawcatuck, R.I., USA) or a twin screw compoundingextruder such as those available from Warner-Pfliederer (Ramsey, N.J.,USA) and Bersdorf Corporation (Charlotte, N.C., USA). Alternatively,loss in weight or volumetric feeders such as those available from K-TronAmerica (Pitman, N.J., USA) may be used to control the composition beingfed to the extruders.

The composite sheet 10 is preferably prepared by an extrusion coatingprocess. In the extrusion coating process, a uniform molten extrudate isfirst coated on the fibrous substrate material. The molten polymer andthe substrate are brought into more intimate contact as the moltenpolymer cools and bonds with the substrate. Such contact and bonding maybe enhanced by passing the layers through a nip formed between tworolls. Alternatively, the molten polymer may be pulled into contact withthe fibrous substrate by passing the coated substrate over a suctioninlet such that the vacuum pulls the molten polymer into contact withthe substrate as the polymer cools and bonds with the substrate. Thebonding may be further enhanced by subjecting the surface of thesubstrate that is to contact the film to surface treatment, such ascorona treatment, as is known in the art and described in ModernPlastics Encyclopedia Handbook, p. 236 (1994), which is herebyincorporated by reference.

One preferred means for applying the film layer 12 to the substrate 14is illustrated in FIG. 3. As can be seen in FIG. 3, the thermoplasticpolymer is fed in pellet form, along with any additives, into the inlet26 of the extruder hopper 24. The polymer is melted and mixed in thescrew extruder 20 at a screw speed in the range of 10 to 200 rpm,depending on the dimensions of the extruder and the properties of thepolymer, and the melted mixture is discharged from the extruder underpressure through the heated line 28 to a flat film die 38. The polymeris discharged at a temperature above the melting temperature of themixture, and preferably at a temperature in the range of 180° to 240° C.The polymer extrusion melt 40 discharging from the flat film die 38coats the fibrous substrate 14.

Preferably, the substrate passes under the die at a speed that iscoordinated with the speed of the extruder so as to obtain a desiredfilm thickness. The coated substrate enters a nip formed between therolls 34 and 36, which rolls are maintained at a temperature selected toobtain a composite sheet with a desired peel strength and moisture vaporpermeability. The temperature of the rolls 34 and 36 is within the rangeof 10° to 120° C. As will be discussed below, higher roll temperatureshave been found to yield a composite sheet with a higher peel strength,while lower roll temperatures have been found to yield composite sheetswith a higher moisture vapor permeability. Preferably, roll 34 is asmooth rubber roller with a low-stick surface coating while the roll 36is a metal roll. A textured embossing roll may be used in place of themetal roll for the roll 36 if a composite sheet with a more texturedfilm layer (and higher surface area) is desired. Passing the coatedsubstrate through the nip formed between cooled rolls 34 and 36 quenchesthe polymer melt while at the same time compressing the polymer melt 40into and against the fibrous substrate 14. The nip pressure should beset high enough that the desired peel strength between the film and thesubstrate is achieved, but not so high that pinholes are formed in thefilm. The cooled polymer forms the film layer 12 of composite sheet 10,which composite sheet is collected on a collection roll 44. If atrilaminate product like that shown in FIG. 2 is desired, an additionalsubstrate material 16 can be laid on the other side of the extrudedpolymer melt 40 as the polymer passes between rolls 34 and 36.

Alternatively, a vacuum process can be applied in order to compress thepolymer melt 40 against the substrate material. The vacuum process issimilar to conventional extrusion coating except that vacuum is used tobond the two substrates instead of nip rolls. The film is sucked intothe fibrous substrate by applying a vacuum force against the undersideof the substrate. The vacuum process optimizes adhesion while alsoproducing products with good loft and hand.

According to another embodiment of the invention, the film layer 12 maybe a moisture vapor permeable, substantially liquid impermeable multiplelayer film structure. Such a film may be coextruded with layerscomprised of the one or more of the above described preferredthermoplastic film materials described herein. Such multiple layermoisture permeable films are disclosed in U.S. Pat. No. 4,725,481(assigned to DuPont), which is hereby incorporated by reference.Multiple layer films are especially useful in the composite sheet of theinvention where it is desirable for the film layer 12 to have differentproperties on its different sides. For example, a composite sheet couldbe made with a bicomponent film layer 12 having one side made of amoisture vapor permeable polymer material that thermally bonds well tothe fibrous substrate 14 and an opposite side comprised of anothermoisture vapor permeable polymer that bonds well to materials to whichthe composite sheet is to be applied. It is anticipated that a moisturevapor permeable film of three or more co-extruded layers could beutilized for the film layer of the composite sheet of the invention inorder to obtain an overall desired set of physical and aestheticproperties for the composite sheet.

The composite sheet 10 is especially useful as a component in disposableabsorbent articles. As used herein, the term “absorbent article” refersto devices which absorb and contain body exudates, and, morespecifically, refers to devices which are placed against or in proximityto the body of the wearer to absorb and contain the various exudatesdischarged from the body. Absorbent articles include disposable diapers,incontinence briefs, incontinence undergarments, incontinence pads,feminine hygiene garments, training pants, pull-on garments, and thelike. The term “disposable” is used herein to describe absorbentarticles which are not intended to be laundered or otherwise restored orreused as an absorbent article (i.e., they are intended to be discardedafter a single use and, preferably, to be recycled, composted orotherwise disposed of in an environmentally compatible manner).Composite sheet 10 has physical properties that make the sheetespecially useful as the outside “backsheet” of a disposable absorbentarticle, which properties include the composite sheet material'spermeability to moisture vapor, its substantial impermeability toliquids, and its strength and durability. The ability of the compositesheet 10 to readily transmit moisture vapor means that hygiene productsincorporating the composite sheet 10 as the product's backsheet materialare comfortable to the wearer. The composite sheet's impermeability tofluids allows the sheet to completely contain bodily fluids even whenthe sheet is subjected to a dynamic impact of the type experienced whena baby or other person wearing a wet absorbent article sits down hard.The strength and durability of the composite sheet 10 permits the sheetto remain intact even after being stretched, rolled and pulled in theprocess of manufacturing an absorbent article.

It is believed that the moisture vapor transmission rate (“MVTR”) of acomposite sheet material used as the backsheet of an absorbent articleis important in reducing humidity and temperature inside the absorbentarticle, thereby reducing the incidence of heat rash and other skinproblems associated with such environmental conditions. For example, inorder to reduce rash inducing humidity and heat buildup within adisposable absorbent article, it has been found that at least a portionof the article's backsheet, and preferably the entire backsheet, shouldhave a moisture vapor transmission rate of at least about 1500 g/m²/24hr., as measured by the desiccant MVTR measurement method described inthe examples below. The composite sheet material of the presentinvention is capable of delivering an MVTR, as measured by the desiccantmethod, of at least about 1500 g/m²/24 hr, and composite sheetsaccording to the invention can deliver an MVTR greater than 4000 g/m²/24hr.

In the composite sheet of the present invention, moisture vaportransmission is enhanced because the moisture permeable film layer 12 isextruded directly onto the nonwoven substrate 14. This direct extrusionimproves moisture transmission for a number of reasons. First, directextrusion makes it possible to make composite sheets with very thin filmlayers, often with an average thickness of less than 30 microns. Thesethin films are highly permeable to moisture vapor but they are stillsubstantially impermeable to liquids. Second, because the film layer ofcomposite sheet 10 is extrusion coated directly onto the substrate 14without the use of an adhesive, there is no adhesive layer to hindermoisture vapor transmission through the composite sheet. Finally, filmlayer 12 is extruded onto substrate 14 and passed through a nip suchthat the film presses into the pores and contours of the substrate. Thisprocess results in a film layer 12 that has a surface facing substrate14 that is highly textured so as to have a high surface area.

A cross section of a sample of the composite sheet material of thepresent invention, made as described in Example 8, was photographed at amagnification level of 500× using a scanning electron microscope (SEM).An SEM photomicrograph of a section of the sample that was 484 micronslong in the direction of the boundary between the film layer 12 and thesubstrate 14 was enlarged and carefully measured using calipers. Thefilm interface had a total length of 871 microns, of which 411 micronsof the interface was adhered directly to fibers of the substrate 14 and460 microns of the interface was open to the pore spaces within thesubstrate. It is believed that the high surface area on the substrateside of the film layer 12 further enhances moisture vapor flux throughthe composite sheet 10.

The composite sheet of the present invention exhibits the importantproperty that it is substantially impermeable to liquids underconditions that are normally associated with the use of absorbentarticles and protective apparel. The liquid impermeability of thecomposite sheet 10 has been characterized according to a number oftests, including a liquid moisture seepage test, a dynamic barrier test,and a microbial barrier test.

The liquid moisture seepage test visually demonstrates the substantialliquid impermeability of the composite sheet 10. As described in theexample below, this test determines whether a solution of food dye,isopropyl alcohol and water passes through a sheet material. As can beseen in Examples 8-17 below, the dye in alcohol solution did not passthrough the composite sheet 10 of the present invention. On the otherhand, when the same test was conducted on a sheet comprised of amicroporous film laminated to a nonwoven substrate, dye solution seepagewas apparent (Comparative Example 1).

The dynamic fluid impact test demonstrates the ability of the compositesheet 10 to resist liquid transmission when used as a backsheet in anabsorbent article. The dynamic fluid impact test described in theexamples below is designed to mimic the energy per unit area that aninfant imparts to a diaper backsheet when abruptly going from a standingto a sitting position. Suitable sheet materials for a diaper backsheetshould exhibit substantially zero dynamic fluid transmission (i.e., lessthan 1 g/m²) when subjected to an impact energy of about 1000 joules/m²as is the case for the composite sheet 14 of the invention. Morepreferably, diaper backsheets exhibit substantially zero dynamic fluidtransmission when subjected to an impact energy of 2400 joules/m² ormore. As reported in Examples 8-17 below, these examples of thecomposite sheet of the invention passed less than 0.4 g/m² of water whensubjected to an impact energy of about 2400 joules/m².

The ability of the composite sheet 10 to act as a barrier to liquidsalso prevents the passage of most odors, bacteria, or other microbesthrough the sheet. When a microporous film was tested according to abacteria flux test used for evaluating porous sterile packagingmaterials (ASTM F 1608-95) (Comparative Example 1), the material did notpass this test because bacteria was found to pass through the sheet. Onthe other hand, the composite sheet 10 of the invention, by beingimpermeable to air during a one hour air porosity test (See Gurley Hilldata in Examples 8, 9, 12, 13, 16 and 17), satisfies the microbialbarrier requirement for impermeable sterile packaging materials, as setforth in ISO standard 11607, section 4.2.3.3.

The strength and durability of composite sheet 10 makes this sheetespecially suitable for absorbent articles. This strength and durabilityallow the composite sheet 10 to remain intact even after beingstretched, rolled, compressed and pulled during the process ofmanufacturing an absorbent article. It is also important that thecomposite sheet be strong and durable enough to remain intact whenstretched, pulled and wetted during wearing of an article made usingcomposite sheet 10 as the backsheet. The strength and durability ofcomposite sheet 10 has been characterized in terms of (1) tensilestrength, (2) the degree to which the sheet will stretch before breaking(known as “elongation”), and (3) the amount of force required to peelthe moisture vapor permeable film from the fibrous substrate of thecomposite sheet (known as “peel strength” or “delamination strength”).

Tensile strength is determined by measuring the tensile force requiredto rupture a sample of sheet material. Elongation is a measure of theamount that a sample of sheet material will stretch under tension beforethe sheet breaks. The elongation is the length just prior to breakexpressed as a percentage of the original sample length. Preferably, acomposite sheet material that is to be used as the backsheet in anabsorbent article has a tensile strength of at least 1 N/cm and anelongation of at least 30% in both the machine and cross directions.More preferably, if the composite sheet of the invention is to be usedas the backsheet in an absorbent article, it should have a tensilestrength of more than 1.5 N/cm and an elongation of at least 50% in bothmachine and cross directions. In the composite sheet of the presentinvention, the tensile properties and elongation properties of thecomposite sheet are largely dependent on the tensile and elongationproperties of the fibrous substrate. A sheet material with the preferredtensile strength and elongation remains intact when wrapped aroundrollers at high speed during manufacture of absorbent articles. Theelongation also makes the articles more comfortable to wearers becausethe articles have some give so as to be more conformable to a wearer'sbody shape because a sheet material with this elongation generally hassome elasticity. As can be seen in Examples 8-17 below, the compositesheet 10 of the invention has a tensile strength of about 11 N/cm in themachine direction and 2 N/cm in the cross direction, and an elongationof from 59% to 87% in the machine direction and 67% to 108% in the crossdirection. The preferred polyether block copolymer film of the inventionprovides a degree of elasticity to a composite sheet material that makesthe sheet especially useful in an absorbent article.

Peel strength is a measure of the force required to delaminate themoisture permeable film from the fibrous substrate of a composite sheet.When the composite sheet 10 is used as a backsheet in a disposableabsorbent article, such as a diaper, it is important that the compositesheet have a peel strength of at least 0.15 N/cm, and more preferably atleast 0.20 N/cm, so that the sheet will not delaminate duringmanufacture of the article or during use. Such a peel strength isespecially difficult to achieve when an adhesive is not used to attachthe moisture vapor permeable film to the fibrous substrate. Good peelstrength is even more difficult to achieve when the moisture vaporpermeable film is chemically incompatible with the fibrous substrate, asis the case when a moisture permeable film comprised solely of apolyether ester block copolymer is coated on a polyolefin-basedsubstrate. “Compatibility” of thermoplastic materials is anart-recognized term that refers, generally, to the degree to which thethermoplastic materials are miscible and/or interact with each other.Similarly, “incompatible” materials, as used herein, means polymermaterials that are substantially immiscible or do not interact with eachother. Incompatible materials do not wet each other well, nor do theyadhere well to each other, even when heated.

Applicants have found that it is possible to greatly improve the peelstrength between a moisture permeable film and a fibrous substrate byoptimizing the physical bonding between the film and the substrateand/or by making the film and the substrate more chemically compatible.As is apparent in Examples 8-17 below, the composite sheet of theinvention generally has a peel strength of from 0.3 N/cm to 0.6 N/cm,and a peel strength as high as a full bonding strength greater than 0.75N/cm, which is the degree of bonding above which the film or thesubstrate will rupture before delamination occurs.

It has been found that physical bonding of the moisture vapor permeablefilm and the fibrous substrate can be greatly enhanced by selectingmaterials and bonding conditions that encourage the polymer film tophysically bind with the fibers of the fibrous substrate. It has beenespecially surprising to find that good peel strength between the filmand substrate can be attained by improving the physical bonding betweenthe film and substrate layers, even where the layers are not chemicallycompatible and the molten polymer of the moisture vapor permeable filmis a poor wetting agent for the fibrous substrate.

It has been found that the use of highly fibrous substrate materials,such as a carded web, improves physical bonding between the film andsubstrate layers of the composite sheet 10. It has also been found thatthe use of a polymer for the film layer that is sufficiently fluid inits molten state to intertwine with the fibers of the substrate, but notso fluid as to run out through the fiber substrate, also improves thepeel strength of the composite sheet.

Extrusion coating and bonding conditions have also been found to have agreat impact on the peel strength between the moisture vapor permeablefilm and the fibrous substrate of the composite sheet. Specificconditions that have been found to have a significant impact on the peelstrength include the temperature of the melt 40 as it exits the die 38,the spacing between the die and the nip, the pressure of the nip, thetemperature of the nip rolls 34 and 36, and the thickness of the filmlaid down on the substrate. It has been found that a polymer melttemperature in the range of 180° to 240° C. promotes excellent bondingof a polyether ester based moisture permeable film to a nonwovenpolyolefin fibrous substrate. These relatively high polymer melttemperatures are thought to decrease the viscosity of the polymer filmat the nip such that more of the film's polymer penetrates into thefibrous substrate as the composite sheet passes through the nip.Minimizing the spacing between the die and the nip has also been foundto improve bonding in the composite sheet. It is postulated that thedecreased die to nip spacing helps to maintain the elevated temperatureof the polymer film layer as the film layer enters the nip so as toimprove physical bonding between the film and substrate layers in thenip for the reasons just discussed above. As can be seen in Examples18-35, a die to nip spacing of about 9 cm can be used to produce acomposite sheet with good peel strength, depending upon the otherprocessing conditions applied.

The bonding conditions at the nip itself should also be controlled so asto improve the physical bonding between the moisture permeable film andthe fibrous substrate. As can be seen in Examples 25 and 31, when otherbonding conditions are kept the same, an increase in the pressureapplied at the nip improves the peel strength of the composite sheet.Maintaining the nip rolls at a temperature greater than ambienttemperature in the range of 40° to 110° C. has also been found toimprove physical bonding between the layers of the composite sheetmaterial. As can be seen in Examples 28, 29 and 30, increasing thetemperature of the rolls 34 and 36 (FIG. 3) improves the peel strengthof the composite sheet when other bonding conditions are kept constant.Applicants believe that the elevated temperature of the nip rolls helpsto keep the moisture vapor permeable film layer fluid enough that thesubstantial pressure applied at the nip will cause the polymer of thefilm to more effectively penetrate into the void spaces in the fibroussubstrate and become more effectively entangled with the substrate.

Physical bonding of moisture permeable film layer 12 to fibroussubstrate 14 has been found to improve with film thickness. Applicantsbelieve that this improvement is a result of the thicker film's betterability to retain heat during the bonding process which serves todecrease the viscosity of the moisture permeable polymer film materialas it enters the nip. As discussed above, it is believed that a lessviscous and more fluid film more easily penetrates the substrate tointertwine with substrate fibers before solidifying. However, thickerfilms tend to have lower moisture vapor transmission rates and they arealso more expensive to produce. Thus, the peel strength that can begained by making the moisture permeable film layer 12 thicker must bebalanced against possible loss in moisture vapor transmission and theadded expense of a thicker film. It is believed that at a given filmthickness, the use of a lower basis weight fibrous substrate materialshould also help to increase peel strength.

The chemical interaction between the moisture permeable film layer 12and the fibrous substrate 14 appears to impact both physical andchemical bonding between the layers of the composite sheet. If thepolymers of the film layer 12 and the substrate 14 are chemicallycompatible, the polymer of the film layer will wet the polymer of thefibers to a greater extent, which, in turn, improves physical bondingbetween the layers of the composite sheet. Making the polymers of themoisture permeable film layer and the fibrous substrate more compatiblealso increases the level of chemical attraction between the layers ofthe composite sheet.

Chemical interaction of the moisture vapor permeable film and thefibrous substrate is enhanced by selecting film materials and substratematerials that are compatible with each other. The preferred polyetherblock copolymer moisture permeable films are compatible with ester-basedfibrous substrates, such as polyester webs, and thus adhere well topolyesters. However, such polyether-based block copolymer films are notchemically compatible with the stronger and less costly polyolefin websthat are more suitable for use in disposable absorbent articles. It hasunexpectedly been found that the addition of a relatively small amountof certain select thermoplastic polymer materials to the polyether blockcopolymer can dramatically improve bonding between a polyether blockcopolymer film and an otherwise incompatible substrate, such as apolyolefin-based web, without unduly impacting the liquidimpermeability, the moisture vapor transmission ability, or the strengthand durability of the film. It has been found that a thermoplasticpolymer can be mixed with a polyether block copolymer to make itpossible to better extrude the polyether copolymer directly onto fibroussubstrates not ordinarily compatible with a copolyether block copolymerand obtain excellent bonding between the film and substrate layerswithout the application of an additional adhesive or bonding agent.

A suitable apparatus for combining the block polyether copolymer(referred to below as “Fraction A”) and a thermoplastic (referred tobelow as “Fraction B”) that is compatible with the substrate 14, isillustrated in FIG. 3. Fraction A and Fraction B are mixed by physicallyblending pellets of Fraction A and Fraction B and then pouring themixture into the inlet 26 of extruder hopper 24. The pellets are fedinto a heated screw extruder 20 where they are melted and further mixed.Fractions A and B are ordinarily not compatible with each other suchthat Fraction B will not by itself distribute well through Fraction A asis required for good uniform moisture vapor transmission properties offilm layer 12 and good uniform adhesion between layer 12 and the fibroussubstrate layer 14. However, it has been found that the addition of asmall amount of certain compatibilizers can greatly improve the mixingof Fractions A and B.

Preferably, the compatibilizer is a thermoplastic material that servesto improve the processing and uniformity of the mixture of Fractions Aand B. The compatibilizer has a character that makes it simultaneouslysoluble or reactive with Fraction B and interactive with Fraction A,thereby producing a dispersion of globules of Fraction B which areadhered to the Fraction A matrix. The compatibilizer (hereinafter“Fraction C”) is chosen according to the nature of Fraction B. FractionC should have a backbone that is compatible with, and is preferablyidentical to, Fraction B and a functional group that is compatible withor interacts with Fraction A. The addition of Fraction C changes themorphology of the composition of the mixture such that Fraction Bdistributes uniformly in Fraction A in the form of globules that arechemically and/or physically bonded to the Fraction A matrix.

Fraction A consists of at least 50% by weight of a block copolyetherester, a block copolyether amide, a polyurethane, or a combinationthereof. Preferred copolyether ester block copolymers for Fraction A aresegmented elastomers having soft polyether segments and hard polyestersegments, as disclosed in U.S. Pat. No. 4,739,012 (assigned to DuPont),such as the polyether ester block copolymers sold by DuPont under thename Hytrel®. Suitable copolyether amide copolymers for use in theFraction A include copolyamides available under the name Pebax® fromAtochem Inc. of Glen Rock, N.J. Suitable polyurethanes for use inFraction A include thermoplastic urethanes available under the nameEstane® from The B.F. Goodrich Company of Cleveland, Ohio. The amount ofFraction A in the polymer mixture will vary depending upon thecomposition of the polymer comprising Fraction A, the type of polymercomprising Fraction B, the desired level of moisture vapor permeability,the desired level of bonding between the film and substrate layers, andthe desired film toughness. Fraction A is typically present in the filmlayer of the composite sheet structure of the invention in an amountranging from 50% to 95% by weight, and more preferably from 70% to 85%by weight.

Fraction B is typically present in the film layer of the composite sheetstructure of the instant invention in an amount ranging from 5% to 50%by weight, and more preferably between 15% and 30% by weight. Fraction Bis preferably a homopolymer of an alpha-olefin, a copolymer or aterpolymer containing an alpha-olefin and one or more other monomers, ora block copolymer of a vinylarene and a conjugated diene. Fraction B mayalso be a blend of these homo-, co- and terpolymers. The selection ofthe compound for Fraction B is dependent on the composition of thefibrous material in the substrate 14. For example, if the substratematerial is primarily polyethylene, the composition of Fraction B shouldcontain an amount of polyethylene sufficient to make the film andsubstrate layers more compatible.

Where Fraction B is a homopolymer, the homopolymer preferably containsthe repeating unit —(R—CH—CH₂)— in which R is hydrogen or an alkylradical having between 1 and 8 carbon atoms. Preferred homopolymersaccording to the invention are low density polyethylene (PE-LD), linearlow density polyethylene (PE-LLD), high density polyethylene (HDPE),very low density polyethylene (VLDPE) and polypropylene.

Where Fraction B is a co- or terpolymer, it preferably contains therepeating unit —(R—CH—CH₂)— above, with at least one furthermonoethylenically unsaturated monomer (aliphatic or aromatic), thefollowing of which can be cited by way of example: vinyl acetate,styrene, and (meth)acrylic derivatives. This other monomer can representup to 35% by weight of the olefinic copolymer, and more preferably from1% to 10% by weight. Preferred copolymers to be used as Fraction B arecopolymers of ethylene and propylene, ethylene vinyl acetate copolymers,copolymers of ethylene and acrylic derivatives (e.g., copolymers ofethylene, carbon monoxide and n-butyl acrylate, commonly known asEnBACO), copolymers of ethylenically unsaturated carboxylic acidmonomers (e.g., acrylic acid, methacrylic acid, crotonic acid, etc.) orthe neutralized metallic salts thereof (as found in the partiallyneutralized ethylene/carboxylic acid copolymers which are commonlyreferred to in the art as ionomers). Fraction B may also compriseterpolymers based on olefin, methyl acrylate and ethyl acrylate or evenmixtures of straight chain and low density polyolefins. Where Fraction Bis a block copolymer of a vinylarene and a conjugated diene, it may havethe general structure A-B-A wherein the two terminal polymer blocks Acomprise thermoplastic polymer blocks of vinylarenes such aspolystyrene, while block B is a polymer block of selectivelyhydrogenated conjugated diene such as isoprene or butadiene. Theproportion of the thermoplastic terminal blocks to the centerelastomeric polymer block and the relative molecular weights of each ofthese blocks is balanced to obtain a rubber having an optimumcombination of properties such that it behaves as a vulcanized rubberwithout requiring the actual step of vulcanization. Such compounds arecommonly referred to as S-EB-S block copolymers and are available fromShell Chemical Company under the name Kraton®. Kraton® is a registeredtrademark of Shell Oil Company. Optionally, these block copolymers canbe grafted with maleic anhydride so as to form adducts which contain0.1% to 10% by weight, preferably 0.2% to 5%, of maleic anhydride (seeU.S. Pat. No. 4,578,429).

The compatibilizer of Fraction C is typically present in the film layerof the composite sheet structure of the invention in an amount rangingfrom 0.1% to 15% by weight, and more preferably between 1% and 8% byweight. Preferred backbones for Fraction C include low densitypolyethylene (PE-LD), linear low density polyethylene (PE-LLD), highdensity polyethylene (HDPE), very low density polyethylene (VLDPE) andpolypropylene. The reactive group of Fraction C may be a graftingmonomer that is grafted to this backbone, and is or contains at leastone alpha- or beta-ethylenically unsaturated carbonic acid or anhydride,or a derivative thereof. Examples of such carboxylic acids andanhydrides, which may be mono-, di- or polycarboxylic acids, are acrylicacids, methacrylic acid, maleic acid, fumaric acid, itaconic hydride,maleic anhydride and substituted maleic anhydride (e.g., dimethyl maleicanhydride). Examples of derivatives of the unsaturated acids are salts,amides, imides and esters (e.g., mono- and disodium maleate, acrylamide,maleimide and diethyl fumarate). Maleic anhydride is a preferredgrafting monomer for the reactive group of Fraction C. The grafting ofthe polymers can be carried out in the melt state, in solution or insuspension. The melt viscosity of the grafted polymer is not restricted,however, most effective alloying is found if the melt index, measured at2.16 kg and 190° C., is between 1 and 15 g/10 min. Such grafted polymerscan be prepared as known in the art.

In addition to the above fractions, the film layer in sheet structuresaccording to the invention may contain conventional additives, such aspigments and fillers (e.g. TiO₂, calcium carbonate, silicas, clay, talc)and stabilizers, such as antioxidants and ultraviolet absorbers. Theseadditives are used for a variety of purposes, including reducing thecost of the film layer of the composite sheet structure, and alteringthe morphology of the film layer of the sheet structure. However, suchadditives have been found to reduce moisture vapor transmission throughthe sheet structure. It is important to maintain the amount of additivein the film at a level that does not result in a moisture vaportransmission rate for the sheet that falls outside of the range requiredfor a particular application. The film layer may be comprised of between0.01% and 30% of additive material, and more preferably between 0.5 and7% of an inert filler material.

A preferred embodiment of an absorbent article incorporating thecomposite sheet of the present invention is the diaper 50, shown in FIG.4. As used herein, the term “diaper” refers to an absorbent articlegenerally worn by infants and incontinent persons that is worn about thelower torso of the wearer. FIG. 4 is a plan view of the diaper 50 of thepresent invention in its flat-out, uncontracted state (i.e., withelastic induced contraction pulled out) with portions of the structurebeing cut-away to more clearly show the construction of the diaper 50.As shown in FIG. 4, the diaper 50 preferably comprises a containmentassembly 70 comprising a topsheet 49; a backsheet 47 joined to thetopsheet; and an absorbent core 75 positioned between the topsheet 49and the backsheet 47. The absorbent core 75 has a pair of opposinglongitudinal edges, an inner surface and an outer surface. The diaperpreferably further comprises elastic leg features 72; elastic waistfeatures 74; and a fastening system 76 preferably comprising a pair ofsecurement members 77 and a landing member 78.

The diaper 50 is shown in FIG. 4 with the portion of the diaper 50 whichfaces the wearer, the inner surface 73, facing the viewer. The diaper 50is shown in FIG. 4 to have an inner surface 73 (facing the viewer inFIG. 4), an outer surface 71 opposed to the inner surface 73, a rear orback waist region 45, a front waist region 46 opposed to the rear waistregion 45, a crotch region 48 positioned between the rear waist region45 and the front waist region 46, and a periphery which is defined bythe outer perimeter or edges of the diaper 46 in which the longitudinalor side edges are designated 50 and the end edges are designated 52. Theinner surface 73 of the diaper 50 comprises that portion of the diaper50 which is positioned adjacent to the wearer's body during use (i.e.,the inner surface 73 generally is formed by at least a portion of thetopsheet 49 and other components joined to the topsheet 49). The outersurface 71 comprises that portion of the diaper 50 which is positionedaway from the wearer's body (i.e., the outer surface 71 is generallyformed by at least a portion of the backsheet 47 and other componentsjoined to the backsheet 47). As used herein, the term “joined”encompasses configurations whereby an element is directly secured to theother element by affixing the element directly to the other element, andconfigurations whereby the element is indirectly secured to the otherelement by affixing the element to intermediate member(s) which in turnare affixed to the other element. The rear waist region 45 and the frontwaist region 46 extend from the end edges 52 of the periphery to thecrotch region 48.

The diaper 50 also has two centerlines, a longitudinal centerline 100and a transverse centerline 110. The term “longitudinal”, as usedherein, refers to a line, axis, or direction in the plane of the diaper50 that is generally aligned with (e.g. approximately parallel with) avertical plane which bisects a standing wearer into left and righthalves when the diaper 50 is worn. The terms “transverse” and “lateral”,as used herein, are interchangeable and refer to a line, axis ordirection which lies within the plane of the diaper that is generallyperpendicular to the longitudinal direction (which divides the wearerinto front and back body halves).

FIG. 5 shows a simplified plan view of the diaper 50 of FIG. 4 depictingthe various panels and their positioning with respect to each other. Theterm “panel” is used herein to denote an area or element of the diaper.(While a panel is typically a distinct area or element, a panel maycoincide (functionally correspond) somewhat with an adjacent panel.) Thediaper 50 has a crotch region 48 comprising a main panel 80 and a pairof leg panels 82; a front waist region 46 comprising a central panelcomprising a medial panel 86 and a waistband panel 88, and side panels90; and a rear waist region 45 comprising a central panel comprising amedial panel 86′ and a waistband panel 88′, and side panels 90′. Themain panel 80 is the portion of the diaper 50 from which the otherpanels emanate. The absorbent core is generally positioned within themain panel 80 since exudates are typically discharged in this region ofthe diaper although the absorbent core will also likely extend into themedial panels 86 and 86′. A leg panel 82 extends generally laterallyoutwardly from and along each side edge 81 of the main panel 80. Eachleg panel 82 generally forms at least a portion of the elastic legfeature. In the front waist region 46, the medial panel 86 of thecentral panel extends generally longitudinally outwardly from and alongthe lateral edge 85 of the main panel 80. The waistband panel 88 extendsgenerally longitudinally outwardly from and along the medial panel 86.The side panels 90 each extend generally laterally outwardly from andalong the central panel. In the rear waist region 44, the medial panel86′ of the central panel extends generally longitudinally outwardly fromand along the lateral edge 85 of the main panel 80. The waistband panel88′ extends generally longitudinally outwardly from and along the medialpanel 86′. The side panels 90′ each extend generally laterally outwardlyfrom and along the central panel.

Referring again to FIG. 4, the containment assembly 70 of the diaper 50is shown as comprising the main body (chassis) of the diaper 50. Thecontainment assembly 70 preferably comprises a topsheet 49, a backsheet47 and an absorbent core 75 having a pair of opposing longitudinaledges, an inner surface, an outer surface. The inner surface of theabsorbent core generally faces the body of the wearer while the outersurface generally faces away from the body of the wearer. When theabsorbent article comprises a separate holder and a liner, thecontainment assembly 70 generally comprises the holder and the liner(i.e., the containment assembly 70 comprises one or more layers ofmaterial to define the holder while the liner comprises an absorbentcomposite such as a topsheet, a backsheet, and an absorbent core.) Forunitary absorbent articles, the containment assembly 70 preferablycomprises the topsheet 49, the backsheet 47 and the absorbent core 75 ofthe diaper with other features added to form the composite diaperstructure.

FIG. 4 shows a preferred embodiment of the containment assembly 70 inwhich the topsheet 49 and the backsheet 47 have length and widthdimensions generally larger than those of the absorbent core 75. Thetopsheet 49 and the backsheet 47 extend beyond the edges of theabsorbent core 75 to thereby form the periphery of the diaper 50. Whilethe topsheet 49, the backsheet 47, and the absorbent core 75 may beassembled in a variety of well known configurations, exemplarycontainment assembly configurations are described generally in U.S. Pat.No. 3,860,003 entitled “Contractible Side Portions for DisposableDiaper” which issued to Kenneth B. Buell on Jan. 14, 1975; U.S. Pat. No.5,151,092 entitled “Absorbent Article With Dynamic Elastic Waist FeatureHaving A Predisposed Resilient Flexural Hinge” which issued to KennethB. Buell et al., on Sep. 29, 1992; and U.S. Pat. No. 5,385,500 entitled“Absorbent Articles Providing Sustained Dynamic Fit” which issued toLaVon et al., on Oct. 25, 1994; each of which is incorporated herein byreference.

In the embodiment shown in FIG. 4, the backsheet 47 preferably comprisesa continuous sheet or layer which defines the front waist region 46, therear waist region 45, and the crotch region 48. As used herein, the term“layer” does not necessarily limit the element to a single strata ofmaterial in that a layer may actually comprise laminates or combinationsof sheets or webs of the requisite types of materials. The backsheet 47has an inner surface and an opposed outer surface. The inner surface isthat portion of the backsheet 47 which is positioned adjacent theabsorbent core. The outer surface of the backsheet 47 corresponds to theouter surface 71 of the diaper 50. Since the backsheet 47 preferablydefines the front waist region 46, the rear waist 45, and the crotchregion 48, the backsheet 47 also has corresponding regions and panels aspreviously defined. (For simplicity, these regions and panels aredenoted in the drawings by the same reference numerals as thecorresponding diaper regions and panels as shown in FIG. 5.)

In the embodiment shown in FIG. 4, the absorbent core is positioned inthe main panel 80, since exudates are typically discharged in thisregion and extends into the medial panels 86 and 86′. In the embodimentshown in FIG. 4, the absorbent core does not extend into the leg panels82, the waistband panels 88 and 88′, or the side panels 90 and 90′. Inother embodiments, the absorbent core may extend into all or some of theleg panels 82, the waistband panels 88 and 88′, and the side panels 90and 90′.

The backsheet 47 of the present invention is that portion of the diaper50 which is generally positioned away from the wearer's skin and whichprevents the exudates absorbed and contained in the absorbent core 75from wetting articles which contact the diaper 50 such as bedsheets andundergarments. Thus, the backsheet 47 is substantially impervious tofluids (e.g., urine). In addition to being fluid impervious, thebacksheet 47 is also permeable to moisture vapor. For disposablediapers, moisture vapor permeability has been found to be critical toperformance especially in hot and humid conditions. When an absorbentarticle is positioned on a wearer, the skin is occluded by the materialsmaking up the absorbent article. This occlusion of the skin, especiallyin hot and humid conditions, prevents evaporation and the resultingcooling of the occluded area. The resultant perspiration raises therelative humidity of air inside of the absorbent article resulting inless comfort for the wearer and perceived negative benefits bycaregivers. In order to reduce humidity and heat buildup within thedisposable diaper, it has been found that at least a portion of thebacksheet 47, and more preferably the entire backsheet 47, should have amoisture vapor transmission rate of at least about 1500 g/m²/24 hr., andpreferably at least about 2500 g/m²/24 hr, and even more preferably atleast about 4000 g/m²/24 hr. As discussed above, the composite sheet 10of the present invention has an ideal moisture vapor transmission ratefor use as a backsheet in a disposable absorbent article, such as thedisposable diaper 50 of FIG. 4. For such an application, the compositesheet 10 is employed with the film layer 12 forming the inner orcore-facing portion of the backsheet and the substrate 14 forming theouter or garment-facing portion of the backsheet.

The backsheet 47 comprised of the composite sheet 10 is preferablypositioned adjacent the outer surface of the absorbent core 75 and ispreferably joined thereto by any suitable attachment means known in theart for bonding such materials. For example, the backsheet 47 may besecured to the absorbent core 75 by a uniform continuous layer ofadhesive, a patterned layer of adhesive, or an array of separate lines,spirals, or spots of adhesive. An example of a suitable attachment meanscomprising an open pattern network of filaments of adhesive is disclosedin U.S. Pat. No. 4,573,986 entitled “Disposable Waste-ContainmentGarment”, which issued to Minetola et al. on Mar. 4, 1986. Anothersuitable attachment means comprising several lines of adhesive filamentsswirled into a spiral pattern is illustrated by the apparatus andmethods shown in U.S. Pat. No. 3,911,173 issued to Sprague, Jr. on Oct.7, 1975; U.S. Pat. No. 4,785,996 issued to Ziecker, et al. on Nov. 22,1978; and U.S. Pat. No. 4,842,666 issued to Werenicz on Jun. 27, 1989.Each of these patents is incorporated herein by reference.Alternatively, the attachment means may comprise heat bonds, pressurebonds, ultrasonic bonds, dynamic mechanical bonds, or any other suitableattachment means or combinations of these attachment means as are knownin the art.

In terms of approaches to bond the composite sheet material to othercomponents of an absorbent article, and more particularly to bond themoisture vapor permeable, liquid impermeable film layer of the compositesheet to other components, it has been observed that only certainmethods of bonding will form bonds of sufficient strength to surviveforces encountered in normal use particularly after the film layer hasbeen subjected to fluid contact and has absorbed fluid. Without wishingto be bound by theory it is presently believed that the film layers ofinterest in accordance with the present invention provide the desiredsuperior performance properties in terms of moisture vapor transmissiondue to their comparatively high moisture content under in-useconditions. This comparatively high moisture content, however, ispresently believed to have negative implications on the bond strength ofthe bond between certain conventional hot melt adhesives and the filmlayer.

One approach which has proven satisfactory is to utilize apolyurethane-based adhesive in accordance with the conventional adhesiveapplication techniques and equipment generally well known in the art,such as described above. Another approach, which is presently preferred,is to utilize the multiple layer, co-extruded film layer described abovewith reference to the aforementioned and incorporated U.S. Pat. No.4,725,481 to Ostapchenko. In utilizing this multiple layer filmapproach, the multiple layer film structure (in a bi-layer execution) isextruded onto the fibrous substrate material with the comparatively morehydrophobic elastomer layer facing outwardly from the substrate and thecomparatively more hydrophilic elastomer layer facing toward thesubstrate. Typically, for a given thickness the hydrophobic elastomerlayer exhibits a lower MVTR performance than the hydrophilic elastomerlayer due to its comparatively lower moisture content under in-useconditions. However, when employed in a comparatively thin layer, theeffect of the hydrophobic lower moisture content film layer does notsignificantly diminish the MVTR performance of the overall compositesheet. Due to the comparatively low moisture content of the hydrophobicelastomer layer, conventional hot melt adhesives and bonding techniquesmay be utilized to successfully form bonds of adequate strength betweenthe composite sheet and other components of the absorbent article evenwhen the film has been wetted. Accordingly, by utilizing a co-extruded,multiple layer, multi-chemistry film layer a composite sheet can beprovided that exhibits both the desired performance properties for thecomposite sheet of the present invention and can be bonded to othercomponents of absorbent articles via conventional adhesive bondingtechniques. (See Examples 36-39 below.)

Quite unexpectedly, additional performance benefits have been discoveredthrough the use of multiple layer films in composite sheets used inconstructing absorbent articles such as diaper 50. More particularly,the use of a multiple layer film comprising a three-layer structure witha hydrophobic elastomer layer on both facing surfaces surrounding ahydrophilic elastomer layer is believed to deliver improved tactilequalities when extruded onto a fibrous substrate to form a compositesheet. Again without wishing to be bound by theory, it is believed thatthe comparatively lower moisture content of the hydrophobic film layersresults in a drier tactile impression when the fibrous substrate layeris touched or palpated, particularly when the fibrous substrate layer iscomparatively thin. Such a multiple layer (tri-layer) embodiment of acomposite sheet material would therefore provide both an improvedbondability with conventional adhesive techniques and an improvedtactile impression from the side of the fibrous substrate layer.Optionally, as discussed above, truly dual-sided configurations could beconstructed analogously to FIG. 2 wherein the multiple layer/tri-layerfilm structure is faced on both sides with a fibrous substrate layer.Optionally, as discussed above, truly dual-sided configurations could beconstructed analogously to FIG. 2 wherein the multiple layer/tri-layerfilm structure is faced on both sides with a fibrous substrate materialto provide an enhanced tactile impression from both sides. Such anexecution is believed to be particularly desirable for such applicationsas leg cuffs, waistbands, side panels, and other aspects of absorbentarticles such as diapers where a wearer may contact both opposingsurfaces of the composite sheet material.

Embodiments of the present invention are also contemplated wherein theabsorbent core is not joined to the backsheet 47, and/or the topsheet 49in order to provide greater extensibility in the front waist region 46and the rear waist region 45.

The absorbent core 75 may be any absorbent member which is generallycompressible, conformable, non-irritating to the wearer's skin, andcapable of absorbing and retaining fluids such as urine and othercertain body exudates. As shown in FIG. 4, the absorbent core 75 has agarment-facing side, a body-facing side, a pair of side edges, and apair of waist edges. The absorbent core 75 may be manufactured in a widevariety of sizes and shapes (e.g., rectangular, hourglass, “T”-shaped,asymmetric, etc.) and from a wide variety of fluid-absorbent materialscommonly used in disposable diapers and other absorbent articles such ascomminuted wood pulp which is generally referred to as airfelt. Examplesof other suitable absorbent materials include creped cellulose wadding;meltblown polymers including coform; chemically stiffened, modified orcross-linked cellulosic fibers; tissue including tissue wraps and tissuelaminates; absorbent foams; absorbent sponges; superabsorbent polymers;absorbent gelling materials; or any equivalent material or combinationsof materials.

The configuration and construction of the absorbent core 75 may vary(e.g., the absorbent core may have varying caliper zones, a hydrophilicgradient, a superabsorbent gradient, or lower average density and loweraverage basis weight acquisition zones; or may comprise one or morelayers or structures). Further, the size and absorbent capacity of theabsorbent core 75 may also be varied to accommodate wearers ranging frominfants through adults. However, the total absorbent capacity of theabsorbent core 75 should be compatible with the design loading and theintended use of the diaper 50.

One embodiment of the diaper 50 has an asymmetric, modified T-shapedabsorbent core 75 having ears in the front waist region but a generallyrectangular shape in the rear waist region. Exemplary absorbentstructures for use as the absorbent core 75 of the present inventionthat have achieved wide acceptance and commercial success are describedin U.S. Pat. No. 4,610,678 entitled “High-Density Absorbent Structures”issued to Weisman et al. on Sep. 9, 1986; U.S. Pa. No. 4,673,402entitled “Absorbent Articles With Dual-Layered Cores” issued to Weismanet al. on Jun. 16, 1987; U.S. Pat. No. 4,888,231 entitled “AbsorbentCore Having A Dusting Layer” issued to Angstadt on Dec. 19, 1989; andU.S. Pat. No. 4,834,735, entitled “High Density Absorbent Members HavingLower Density and Lower Basis Weight Acquisition Zones”, issued toAlemany et al. on May 30, 1989. The absorbent core may further comprisethe dual core system containing an acquisition/distribution core ofchemically stiffened fibers positioned over an absorbent storage core asdetailed in U.S. Pat. No. 5,234,423, entitled “Absorbent Article WithElastic Waist Feature and Enhanced Absorbency” issued to Alemany et al.,on Aug. 10, 1993; and in U.S. Pat. No. 5,147,345, entitled “HighEfficiency Absorbent Articles For Incontinence Management” issued toYoung, LaVon and Taylor on Sep. 15, 1992. All of these patents areincorporated herein by reference.

The topsheet 49 is preferably positioned adjacent the inner surface ofthe absorbent core 75 and is preferably joined thereto and to thebacksheet 47 by attachment means (not shown) such as those describedabove with respect to joining the backsheet 49 to the absorbent core 47.In a preferred embodiment of the present invention, the topsheet 49 andthe backsheet 47 are joined directly to each other in the diaperperiphery and are indirectly joined together by directly joining them tothe absorbent core 75 by any suitable means.

The topsheet 49 is preferably compliant, soft feeling, andnon-irritating to the wearer's skin. Further, the topsheet 49 ispreferably fluid pervious permitting fluids (e.g., urine) to readilypenetrate through its thickness. A suitable topsheet 49 may bemanufactured from a wide range of materials such as woven and nonwovenmaterials; polymeric materials such as apertured formed thermoplasticfilms, apertured plastic films, and hydroformed thermoplastic films;porous foams; reticulated foams; reticulated thermoplastic films; andthermoplastic scrims. Suitable woven and nonwoven materials can becomprised of natural fibers (e.g., wood or cotton fibers), syntheticfibers (e.g., polymeric fibers such as polyester, polypropylene, orpolyethylene fibers) or from a combination of natural and syntheticfibers. The topsheet 49 is preferably made of a hydrophobic material toisolate the wearer's skin from fluids which have passed through thetopsheet 49 and are contained in the absorbent core 75 (i.e. to preventrewet). If the topsheet 49 is made of a hydrophobic material, at leastthe upper surface of the topsheet 49 is treated to be hydrophilic sothat fluids will transfer through the topsheet more rapidly. Thisdiminishes the likelihood that body exudates will flow off the topsheet49 rather than being drawn through the topsheet 49 and being absorbed bythe absorbent core 75. The topsheet 49 can be rendered hydrophilic bytreating it with a surfactant. Suitable methods for treating thetopsheet 49 with a surfactant include spraying the topsheet 49 materialwith the surfactant and immersing the material into the surfactant. Amore detailed discussion of such a treatment and hydrophilicity iscontained in U.S. Pat. No. 4,988,344 entitled “Absorbent Articles withMultiple Layer Absorbent Layers” issued to Reising, et al on Jan. 29,1991 and U.S. Pat. No. 4,988,345 entitled “Absorbent Articles with RapidAcquiring Absorbent Cores” issued to Reising on Jan. 29, 1991, each ofwhich is incorporated by reference herein. As mentioned in thebackground discussion above, such hydrophilic materials tend to reducethe surface tension of bodily fluids discharged into an absorbentarticle, which increases the likelihood of liquid seepage if there arepores or pinholes in the backsheet of the article.

An alternative preferred topsheet comprises an apertured formed film.Apertured formed films are preferred for the topsheet because they arepervious to body exudates and yet non-absorbent and have a reducedtendency to allow fluids to pass back through and rewet the wearer'sskin. Thus, the surface of the formed film which is in contact with thebody remains dry, thereby reducing body soiling and creating a morecomfortable feel for the wearer. Suitable formed films are described inU.S. Pat. No. 3,929,135, entitled “Absorptive Structures Having TaperedCapillaries”, which issued to Thompson on Dec. 30, 1975; U.S. Pat. No.4,324,246 entitled “Disposable Absorbent Article Having A StainResistant Topsheet”, which issued to Mullane, et al. on Apr. 13, 1982;U.S. Pat. No. 4,342,314 entitled “Resilient Plastic Web ExhibitingFiber-Like Properties”, which issued to Radel. et al. on Aug. 3, 1982;U.S. Pat. No. 4,463,045 entitled “Macroscopically ExpandedThree-Dimensional Plastic Web Exhibiting Non-Glossy Visible Surface andCloth-Like Tactile Impression”, which issued to Ahr et al. on Jul. 31,1984; and U.S. Pat. No. 5,006,394 “Multilayer Polymeric Film” issued toBaird on Apr. 9, 1991. Each of these patents is incorporated herein byreference.

It may also be desirable to provide the disposable absorbent article ofthe present invention with extensibility or elasticity in all or aportion of the side panels 90. (As used herein, the term “extensible”refers to materials that are capable of extending in at least onedirection to a certain degree without undue rupture. The terms“elasticity” and “elastically extensible” refer to extensible materialsthat have the ability to return to approximately their originaldimensions after the force that extended the material is removed. Asused herein, any material or element described as “extensible” may alsobe elastically extensible unless otherwise provided.) Extensible sidepanels 90 provide a more comfortable and contouring fit by initiallyconformably fitting the diaper to the wearer and sustaining this fitthroughout the time of wear well passed when the diaper has been loadedwith exudates since the side panels allow the sides of the diaper toexpand and contract. Extensible side panels 90 further provide moreeffective application of the diaper 50 since even if the diaperer pullsone side panel 90 further than the other during the application(asymmetrically), the diaper 50 will “self-adjust” during wear. Whilethe extensible side panels 90 may be constructed in a number ofconfigurations, examples of diapers with extensible side panels aredisclosed in U.S. Pat. No. 4,857,067, entitled “Disposable Diaper HavingShirred Ears” issued to Wood, et al. on Aug. 15, 1989; U.S. Pat. No.4,381,781 issued to Sciaraffa, et al. on May 3, 1983; U.S. Pat. No.4,938,753 issued to Van Gompel, et al. on Jul. 3, 1990; and in U.S. Pat.No. 5,151,092 issued to Buell et al. on Sep. 29, 1992; each of which areincorporated herein by reference.

The extensible side panels, or any other elements of the diaper 50 inwhich extensibility or elasticity is desirable such as the waistbandsmay comprise materials that have been “prestrained”, or “mechanicallyprestrained” (i.e., subjected to some degree of localized patternmechanical stretching to permanently elongate the material), orstructural elastic-like webs, as described in U.S. Pat. No. 5,518,801issued to Chappell et al. on May 21, 1996. The materials may beprestrained using deep embossing techniques as are known in the art.Alternatively, the materials may be prestrained by directing thematerial through an incremental mechanical stretching system asdescribed in U.S. Pat. No. 5,330,458 issued to Buell et al., on Jul. 19,1994. The materials are then allowed to return to their substantiallyuntensioned condition, thus forming a zero strain stretch material thatis extensible, at least up to the point of initial stretching. Examplesof zero strain materials are disclosed in U.S. Pat. No. 2,075,189 issuedto Galligan on Mar. 30, 1937; U.S. Pat. No. 3,025,199 issued to Harwoodon Mar. 13, 1962; U.S. Pat. Nos. 4,107,364 and 4,209,563 issued toSisson on Aug. 15, 1978 and Jun. 24, 1980, respectively; U.S. Pat. No.4,834,741 issued to Sabee on May 30, 1989; and U.S. Pat. No. 5,151,092issued to Buell et al., on Sep. 29, 1992. All of the above referencedpatents are hereby incorporated by reference.

The diaper 50 preferably further comprises elastic leg features 72 forproviding improved containment of fluids and other body exudates. Eachelastic leg feature 72 may comprise several different embodiments forreducing the leakage of body exudates in the leg panels 82 (the elasticleg feature can be and is sometimes also referred to as leg bands, sideflaps, barrier cuffs, or elastic cuffs.) U.S. Pat. No. 3,860,003describes a disposable diaper which provides a contractible leg openinghaving a side flap and one or more elastic members to provide anelasticized leg cuff (gasketing cuff). U.S. Pat. No. 4,909,803 entitled“Disposable Absorbent Article Having Elasticized Flaps” issued to Azizet al. on Mar. 20, 1990, describes a disposable diaper having “stand-up”elasticized flaps (barrier cuffs) to improve the containment of the legregions. U.S. Pat. No. 4,695,278 entitled “Absorbent Article Having DualCuffs” issued to Lawson on Sep. 22, 1987; and U.S. Pat. No. 4,795,454entitled “Absorbent Article Having Leakage-Resistant Dual Cuffs” issuedto Dragoo on Jan. 3, 1989, describe disposable diapers having dual cuffsincluding a gasketing cuff and a barrier cuff. U.S. Pat. No. 4,704,115entitled “Disposable Waist Containment Garment” issued to Buell on Nov.3, 1987, discloses a disposable diaper or incontinence garment havingside-edge-leakage-guard gutters configured to contain free fluids withinthe garment. Each of these patents is incorporated herein by reference.

While each elastic leg feature 72 may be configured so as to be similarto any of the leg bands, side flaps, barrier cuffs, or elastic cuffsdescribed above, it is preferred that each elastic leg feature 72comprise at least an inner barrier cuff comprising a barrier flap and aspacing element such as described in the above-referenced U.S. Pat. No.4,909,803. In a preferred embodiment, the elastic leg feature 72additionally comprises an elastic gasketing cuff 63 with one or moreelastic strands 65, positioned outboard of the barrier cuff such asdescribed in the above-referred U.S. Pat. No. 4,695,278.

The diaper 50 preferably further comprises an elastic waist feature 74that provides improved fit and containment. The elastic waist feature 74is that portion or zone of the diaper 50 which is intended toelastically expand and contract to dynamically fit the wearer's waist.The elastic waist feature 74 preferably extends longitudinally outwardlyfrom at least one of the waist edges of the absorbent core 75 andgenerally forms at least a portion of the end edge of the diaper 50.Disposable diapers are generally constructed so as to have twoelasticized waistbands, one positioned in the rear waist region and onepositioned in the front waist region, although diapers can beconstructed with a single elasticized waistband. Further, while theelastic waist feature 74 or any of its constituent elements can comprisea separate element affixed to the diaper 50, the elastic waist feature74 may be constructed as an extension of other elements of the diapersuch as the backsheet 47 or the topsheet 49, preferably both thebacksheet 47 and the topsheet 49. Embodiments are also contemplatedwherein the elastic waist feature 74 comprises apertures, as describedabove, to provide breathability in the waist regions. The elastic waistfeature 74 may be constructed in a number of different configurationsincluding those described in U.S. Pat. No. 4,515,595 entitled“Disposable Diapers with Elastically Contractible Waistbands” issued toKievit et al. on May 7, 1985 and the above referenced U.S. Pat. No.5,151,092 issued to Buell; each of these references being incorporatedherein by reference.

The diaper 50 also comprises a fastening system 76 which forms a sideclosure which maintains the rear waist region 45 and the front waistregion 46 in an overlapping configuration such that lateral tensions aremaintained around the circumference of the diaper to maintain the diaperon the wearer. Exemplary fastening systems are disclosed in U.S. Pat.No. 3,848,594 issued to Buell on Nov. 19, 1974; U.S. Pat. No. 4,662,875issued to Hirotsu and Robertson on May 5, 1987; U.S. Pat. No. 4,869,724issued to Scripps on Sep. 26, 1989; U.S. Pat. No. 4,846,815 issued toScripps on Jul. 11, 1989; U.S. Pat. No. 4,894,060 issued to Nestegard onJan. 16, 1990; U.S. Pat. No. 4,946,527 issued to Battrell on Aug. 7,1990; and U.S. Pat. No. 5,326,612 entitled “Nonwoven Female ComponentFor Refastenable Fastening Device And Method of Making the Same” issuedto David J. K. Goulait on Jul. 5, 1994. Each of these patents isincorporated herein by reference.

FIG. 6 shows a plan view of an alternative embodiment of the diaperbacksheet of the present invention, with the portion of the backsheetpositioned adjacent to the absorbent core facing the viewer. As shown inFIG. 6, the backsheet 247 comprises two layers 250 and 252. Layers 250and 252 may be secured together by any suitable attachment means such asthose described above. In this embodiment, layer 250 forms the outersurface of the diaper and layer 252 is positioned adjacent to theabsorbent core. Since layer 250 is that portion of the backsheet 247which will come into contact with the wearer's skin, layer 250 ispreferably soft and comprises a nonwoven web. In addition to being soft,layer 250 is preferably moisture vapor permeable. Layer 250 preferablyexhibits a moisture vapor transmission rate, of at least about 2000g/m²/24 hr., more preferably at least about 2500 g/m²/24 hr. Since layer250 does not need to prevent leakage of exudates absorbed and containedwithin the absorbent core, selection of materials that provide thedesired softness and breathability is quite extensive. Suitablematerials include, but are not limited to, nonwoven webs such asspunbond webs, meltblown webs, carded webs and the like. The nonwovenwebs for layer 250 may comprise synthetic fibers, natural fibers,multi-component fibers such as bi-component fibers, or mixtures andblends thereof.

Layer 252 is the portion of the backsheet 247 which will prevent theexudates absorbed and contained in the absorbent core from wettingarticles which contact the diaper. In order to protect the user againstunwanted leakage of exudates absorbed and contained within the absorbentcore layer 252 should have width and length dimensions greater thanthose of the absorbent core. If layer 252 is not large enough exudatesabsorbed and contained in the absorbent core may find their way throughthe outer layer 250 during normal usage conditions. In the embodimentshown in FIG. 7, the absorbent core is preferably positioned in the mainpanel 80 and extends into the medial panels 86 and 86′. Accordingly,layer 252 is positioned within the main panel 80 and extends into themedial panels 86 and 86′. Layer 252 has length and width dimensions atleast as large as those of the absorbent core and preferably greaterthan those of the absorbent core. If desired, layer 252 may extendbeyond the main panel 80 and the medial panels 86 and 86′ to into theleg panels 82, the waistband panels 88 and 88′, and the side panels 90and 90′. In addition, layer 252 may extend laterally and longitudinallyoutwardly from the main panel 80 to form portions of the periphery ofthe disposable diaper.

While layer 250 provides a substantial amount of moisture vaporpermeability for the diaper, layer 252 should also be moisture vaporpermeable in order to provide additional comfort for the wearer. In theembodiment of the invention shown in FIG. 6, layer 252 is comprised ofthe composite sheet 10 described above.

While a presently preferred embodiment of an absorbent article such asdiaper 50 according to the present invention utilizes a composite sheet10 according to the present invention for substantially the full extentof the backsheet 47, it is to be understood that the absorbent articlesare in no way limited to such an embodiment. For example, a backsheetcould be constructed from multiple backsheet elements having similar ordiverse properties and constructions as described above with regard toFIG. 6. One such approach would be to form a backsheet with an externalfacing surface of a unitary or composite nonwoven layer as a substratewith the film layer comprising only the region of the backsheet wherefluid imperviousness is desired, such as, for example, the regioncorresponding to the region 252 depicted in FIG. 6.

Moreover, it may also be desirable for certain applications to reversethe orientation of the layers 250 and 252 of FIG. 6 so as to place thefilm layer on the external or garment-facing side of the backsheet andthe fibrous substrate layer on the internal or absorbent-core-facingside of the backsheet. It may also likewise be desirable to utilize thecomposite sheet 10 in the dual-sided embodiment of FIG. 2 wherein bothsides of the backsheet would be faced with a fibrous layer. All suchvariations are contemplated as being within the scope of the presentinvention. Moreover, depending upon the specific application, theproperties provided by the composite sheets of the present invention mayalso be employed to great advantage in other regions of the absorbentarticle besides the central portion of the backsheet which overlies theabsorbent core structure. For example, the desirable fluid-impervious,moisture-vapor-pervious properties of the composite sheet also providedesirable attributes for peripheral portions of the absorbent articlewhich extend laterally outwardly from the marginal edges of theabsorbent core such as the side panels 90, 90′ depicted in FIG. 5. Othersuch “peripheral portions” of the absorbent article for which suchattributes may be desirable are in the vicinity of the leg panels 82including but not limited to various bands, cuffs, and flaps.

Likewise, while much of the foregoing discussion as focused upon therepresentative absorbent article in the form of diaper 50, it is to beunderstood that the materials and principles of the present inventionare equally applicable to other absorbent articles such as incontinencebriefs, incontinence undergarments, diaper holders and liners, femininehygiene products (sanitary napkins, pantiliners, etc.), training pants,pull-on garments, and the like wherein the materials of the presentinvention may be employed advantageously. By way of illustration, abacksheet of a sanitary napkin according the present invention could beformed from a composite sheet of the present invention, as couldperipheral portions of a sanitary napkin such as wings or side flaps.

After manufacture of the composite sheet 10, and either before or afterthe sheet's incorporation into an absorbent article, it may be desirableto subject the sheet to a post-formation mechanical process such ascreping, straining/activation by rolling with corrugated rolls, orotherwise. One such representative process is described in detail inU.S. Pat. No. 5,518,801 to Chappell et al., the disclosure of which ishereby incorporated herein by reference.

The following non-limiting examples are intended to illustrate theproduct and process of the invention and not to limit the invention inany manner.

EXAMPLES

In the description above and in the non-limiting examples that follow,the following test methods were employed to determine various reportedcharacteristics and properties. ASTM refers to the American Society forTesting and Materials, TAPPI refers to the Technical Association of Pulpand Paper Industry, and ISO refers to the International Organization forStandardization.

Basis weight was determined by ASTM D-3776, which is hereby incorporatedby reference, and is reported in g/m².

Composite Sheet Thickness was determined by ASTM method D 1777-64, whichis hereby incorporated by reference, and is reported in microns.

Film Thickness, is reported in microns, and was determined as follows:

${{Film}\mspace{14mu}{thickness}} = \frac{\begin{matrix}{\left( {{composite}\mspace{14mu}{sheet}\mspace{14mu}{sample}\mspace{14mu}{weight}} \right) -} \\{\left( {{substrate}\mspace{14mu}{basis}\mspace{14mu}{weight}} \right)\left( {{sample}\mspace{14mu}{area}} \right)}\end{matrix}}{\left( {{sample}\mspace{14mu}{area}} \right)\left( {{density}\mspace{14mu}{of}\mspace{14mu}{film}\mspace{14mu}{material}} \right)}$

Tensile strength was determined by ASTM D 1682, Section 19, which ishereby incorporated by reference, with the following modifications. Inthe test a 2.54 cm by 20.32 cm (1 inch by 8 inch) sample was clamped atopposite ends of the sample. The clamps were attached 12.7 cm (5 in)from each other on the sample. The sample was pulled steadily at a speedof 5.08 cm/min (2 in/min) until the sample broke. The force at break wasrecorded in Newtons/cm as the breaking tensile strength.

Elongation to Break of a sheet is a measure of the amount a sheetstretches prior to failure (breaking) in a strip tensile test. A 1.0inch (2.54 cm) wide sample is mounted in the clamps—set 5.0 inches (12.7cm) apart—of a constant rate of extension tensile testing machine suchas an Instron table model tester. A continuously increasing load isapplied to the sample at a crosshead speed of 2.0 in/min (5.08 cm/min)until failure. The measurement is given in percentage of stretch priorto failure. The test generally follows ASTM D1682-64.

Peel strength is measured according to a test that generally follows themethod of ASTM D 2724-87, which is hereby incorporated by reference. Thetest was performed under two different conditions, both of which used aconstant rate of extension tensile testing machine such as an Instrontable model tester.

According to what we define as test Condition A, which was used inExamples 1-17 and in discussion portion of the specification, a 2.54 cm(1.0 in) by 20.32 cm (8.0 in) sample is delaminated approximately 3.18cm (1.25 in) by inserting a pick into the cross-section of the sample toinitiate a separation and then delaminated by hand. The delaminatedsample faces are mounted in the clamps of the tester which are set 2.54cm (1.0 in) apart. The tester is started and run at a cross-head speedof 5.08 cm/min (2.0 in/min). The computer starts picking up readingsafter the slack is removed in about 1.27 cm (0.5 in) of crossheadtravel. The sample is delaminated for about 15.24 cm (6 in) during whichapproximately 3000 readings are taken and averaged. The averagedelamination strength is given in N/cm. A suitable method for initiatingthe peel is to dip the end of a sample in isopropyl alcohol to swell thesample, begin peeling by hand, and then remove and discard the portionof the sample contacted with the alcohol before measuring peel strength.

According to what we define as test Condition B, which was used inExamples 18-34, the method to test Condition A is used except that thesamples are 15 cm (6 in) long, a crosshead speed of 10 in/min is used,peel is initiated by hand rather than with a pick, and delaminationstrength was recorded from the average indicated on the recording chart.

Moisture Vapor Transmission Rate (MVTR) was determined by one of twotest methods. The first method used follows ASTM E96-B, which is herebyincorporated by reference, and is reported in g/m²/24 hrs.

The second method is referred to as the dessicant method for measuringmoisture vapor transmission rate as set forth below. Briefly summarizingthis method, a known amount of desiccant (CaCl₂) is put into a flanged“cup” like container. The sample material is placed on the top of thecontainer and held securely by a retaining ring and gasket. The assemblyis then weighed and recorded as the initial weight. The assembly isplaced in a constant temperature (40° C.) and humidity (75% RH) chamberfor five (5) hours. The assembly is then removed from the chamber,sealed to prevent further moisture intake, and allowed to equilibratefor at least 30 minutes at the temperature of the room where the balanceis located. The amount of moisture absorbed by the CaCl₂ is determinedgravimetrically and used to estimate the moisture vapor transmissionrate (MVTR) of the sample by weighing the assembly and recording thefinal weight. The moisture vapor transmission rate (MVTR) is calculatedand expressed in g/m²/24 hr. using the formula below. A referencesample, of established permeability, is used as a positive control foreach batch of samples. Samples are assayed in triplicate. The reportedMVTR is the average of the triplicate analyses, rounded to the nearest100. The significance of differences in MVTR values found for differentsamples can be estimated based on the standard deviation of thetriplicate assays for each sample.

Suitable Analytical Balances for performing the measurements include aMettler AE240 or equivalent (300 g capacity) or a Sartorius 2254S0002 orequivalent (1000 g capacity). A suitable sample holding assemblycomprises a cup and retaining ring machined from Delrin® (such as thatavailable from McMaster-Carr Catalog #8572K34) with a gasket made of GCSeptum Material (Alltech catalog #6528). The dessicant comprises CaCl₂for U-tubes, available from Wako Pure Chemical Industries, Ltd.,Richmond, Va. Product # 030-00525. The plastic food wrap comprises SaranWrap, available from Dow Chemical Company, or equivalent.

The CaCl₂ can be used directly from a sealed bottle as long as the sizeof the lumps is such that they do not pass through a No. 10 sieve.Usually the top two-thirds of the bottle do not have to be sieved.However, the bottom third contains fines that should be removed bysieving. The CaCl₂ can be used from a closed container without drying.It can be dried at 200° C. for 4 hours if required.

Exxon Exxaire microporous material, Catalog # XBF-100W, is used as theReference Standard Material. Triplicate samples should be prepared andanalyzed along with each set of test samples as described below.

Representative samples should be obtained from the materials to betested. Ideally, these samples should be taken from different areas ofthe material so as to represent any variations present. Three samples ofeach material are needed for this analysis.

Samples should be cut into rectangular pieces approximately 1.5″×2.5″.If the samples are not uniform, clearly mark the area for whichbreathability is to be evaluated. If the samples are not bidirectional,clearly mark the side that is to be exposed to high humidity. Forsamples used in diapers and catamenials, this is usually the side thatcontacts the skin.

To begin a test session, (1) weigh 15.0±0.02 grams of CaCl₂ and place inthe MVTR cup. Gently tap the cup 10 times on the bench top to distributeand lightly pack the CaCl₂. The CaCl₂ should be level and about 1 cmfrom the top of the cup. Then (2) place the sample, with the highhumidity side up (if required), over the opening in the top of the cup.Make sure that the sample overlaps the opening so that a good seal willbe obtained. Next, (3) place the gasket material and the retaining ringon the top of the cup, aligning the screw holes and checking to makesure that the sample has not moved. Tighten the screws to securelyfasten the retaining ring and seal the sample to the top of the cup.Care should be taken to not over tighten the screws as this leads todistortion of some samples. If distortion of the sample occurs, loosenthe screws and tighten again. Then (4) weigh the MVTR cup assembled instep 3. Record this weight as the initial weight.

After weighing the assembly, (5) place the sample in the CT/CH chamberfor 5.0 hours (to the nearest minute). When the time has elapsed, (6)remove the sample from the CT/CH chamber, tightly cover it with plasticwrap secured by a rubber band. Record the time of sample removal towithin the nearest minute. Allow samples to equilibrate for at least 30minutes at the temperature of the room where the balance is located.After equilibration, (7) remove the Saran wrap and weigh the cup. Recordthis weight as the final weight.

The MVTR is then calculated in units of g H₂O/24 hr/m² using theformula:

${MVTR} = \frac{\left( {{{final}\mspace{14mu}{weight}} - {{initial}\mspace{14mu}{weight}}} \right) \times 24.0}{{{area}\mspace{14mu}{of}\mspace{14mu}{sample}\mspace{14mu}{in}\mspace{14mu}{meters} \times 5.0\mspace{14mu}\left( {{time}\mspace{14mu}{in}\mspace{14mu}{chamber}} \right)}\mspace{14mu}}$where:

-   -   24.0 is used to convert the data to the 24 hour basis;    -   the area of sample is equal to the open area of the mouth of the        cup; and    -   5.0 is the duration of the test in hours

Calculate the average MVTR for each set of triplicate samples and thereference standard. Round the average MVTR for the reference standard tothe nearest 100. If the MVTR for the reference standard is in the rangeof 4000 to 4600, it is in the acceptable quality control range and theresults for that day can be reported. Round the average MVTR for eachsample set to the nearest 100. Report this value as the MVTR for thesample of material. Steps 1 through 7 are repeated for the triplicateanalyses of each sample and the reference standard. Typically, multiplesamples are processed in parallel.

Dynamic Fluid Transmission is measured with the apparatus 100 shown inFIG. 7. According to this test, an absorption material 102 weighed tothe nearest 0.0001 gram is placed directly on top of the energyabsorbing impact pad 103. The absorption material 102 may comprise a No.2 filter paper available from Whatman Laboratory Division, Distributedby VWR Scientific of Cleveland, Ohio. The absorption material should beable to absorb and retain simulated urine which passes through the sheetmaterial being tested. The energy absorbing impact pad 103 is a carbonblack filled cross linked rubber foam. The 5 inch by 5 inch squareimpact pad has a density of 0.1132 g/cm³ and a thickness of 0.3125inches. The impact pad 103 has a Durometer Value of A/30/15 according toASTM 2240-91. A circular absorbent core material 104 measuring 0.0635meters (2.5 inches) in diameter is weighed. The absorbent core materialmay comprise individualized, crosslinked wood pulp cellulosic fibers asdescribed in U.S. Pat. No. 5,137,537 issued to Herron et al. on Aug. 11,1992. The absorbent core material should be able to hold a sufficientamount of simulated urine, e.g., at least about ten times its dryweight. The absorbent core has a basis weight of about 228 g/m². Theabsorbent core material is then is loaded with simulated urine to aboutten (10) times its dry weight. The simulated urine is an aqueouscomposition, maintained at 37° C., and comprised of the followingcomponents dissolved in distilled water: 2.0 μL KCl; 2.0 g/L Na₂SO₄;0.85 g/L (NH₄)H₂PO₄; 0.15 g/L (NH₄)₂H₂PO₄; 0.19 g/L CaCl₂; and 0.23 g/LMgCl₂.

A section of the backsheet material 105 to be tested is placed face downwith the outside surface on a clean and dry tabletop. The loaded corematerial 104 is placed directly in the center of the backsheet material105. The backsheet/core arrangement is then secured to the impactportion 107 of the impact arm 108 with a rubber band 109. Thebacksheet/core arrangement is positioned such that the core 104 isadjacent the bottom surface 110 of the impact portion 107. The impactarm 108 is raised to a desired impact angle to provide the desiredimpact energy. The impact arm 108 is dropped and the impact arm 108 isthen immediately (about 1 second after impact) raised and the filterpaper 102 is removed and placed on a digital scale. The mass of the wetfilter paper is then recorded at the three minute mark. The dynamicfluid transmission value (DFTV) is calculated and expressed in g/m²using the following formula:

${DFTV} = \frac{\begin{matrix}{{{mass}\mspace{14mu}{of}\mspace{14mu}{the}\mspace{14mu}{wet}\mspace{14mu}{filter}\mspace{14mu}{paper}\mspace{14mu}({grams})} -} \\{{mass}\mspace{14mu}{of}\mspace{14mu}{the}\mspace{14mu}{dry}\mspace{14mu}{filter}\mspace{14mu}{paper}\mspace{14mu}({grams})}\end{matrix}}{{impact}\mspace{14mu}{area}\mspace{14mu}\left( m^{2} \right)}$The impact area, expressed in m², is the area of the bottom surface 110of the impact portion 107. The impact area is 0.00317 m². The absorbentcore material 104 should have an area slightly larger than that of theimpact area of the surface 110.

Gurley Hill Porosity is a measure of the barrier strength of the sheetmaterial for gaseous materials. In particular, it is a measure of howlong it takes for a volume of gas to pass through an area of materialwherein a certain pressure gradient exists. Gurley-Hill porosity ismeasured in accordance with TAPPI T-460 om-88 using a Lorentzen & WettreModel 121D Densometer. This test measures the time of which 100 cubiccentimeters of air is pushed through a one inch diameter sample under apressure of approximately 4.9 inches of water. The result is expressedin seconds and is usually referred to as Gurley Seconds.

Microbial Barrier for Sterile Packaging is measured according to ISO11607 which states under section 4.2.3.2 that a material that isimpermeable to air for one hour (according to an air porosity test)satisfies the standard's microbial barrier requirements. With regard toporous materials, section 4.2.3.3 of ISO 11607 states that there is nouniversally applicable method of demonstrating microbial barrierproperties in porous materials; but notes that the microbial barrierproperties of porous materials is typically conducted by challengingsamples with an aerosol of bacterial spores or particulates under a setof test conditions which specify the flow rate through the material,microbial challenge to the sample, and duration of the test. One suchrecognized test is ASTM F 1608-95.

Liquid Moisture Seepage is detected using a solution of 70 partsisopropyl alcohol, 30 parts water and 1 part red dye food color.According to this test, a sheet of a white absorbent blotting materialmeasuring about 89 cm by 61 cm (35 in by 24 in) is placed on a flatsurface and covered with a test sample of the same dimensions with thesubstrate side of the sample facing up. A 250 ml portion of the solutionis poured on top of the test sample and covered with a templatemeasuring about 46¾ cm by 46¾ cm (18 in by 18 in). A 4.5 kg (10 lb)weight is placed on top of the template for 10 minutes after which theweight, template and test sample are removed from the white blottingpaper. The paper is then inspected for ink spots to determine whetherseepage occurred.

Example 1

A composition was prepared by dry blending 86% by weight of acopolyether ester thermoplastic elastomer (Hytrel® 4778 obtained fromDuPont) with 4% by weight of a UV stabilizer concentrate (Hytrel® 20UV,obtained from DuPont), 4% by weight of a heat stabilizer concentrate(Hytrel® 30HS obtained from DuPont), and 6% by weight of a maleicanhydride modified polyolefin copolymer (Fusabond® 373 obtained fromDuPont Canada). Fusabond® is a registered trademark of DuPont Canada.The composition was fed to a melt extrusion coating line including asingle screw extruder with an attached mixing head. The screw extruderwas made by Egan Division of Davis-Standard Corporation. The heatingzones of the extruder heat the polymer to a temperature above itsmelting point. The melted polymer mixture was fed to a film die with awidth of about 90 cm that was maintained at about 220° C. The polymerwas laminated onto a corona treated nonwoven polypropylene textilematerial (Typar® thermobonded polypropylene obtained from DuPont) at aline speed of 18.3 m/min. The polymer melt and nonwoven textile materialwere passed through a pair of nip rolls (one rubber faced roll againstthe nonwoven textile material and one steel faced roll against thepolymer melt). The resulting laminate had a coating thickness of about25 microns and peel strength values of 0.063 N/cm in the machinedirection (MD) and 0.032 N/cm in the cross direction (CD) and an MVTRvalue of 700 g/m²/24 hr (by method ASTM E96-B).

Example 2

The Typar® nonwoven fabric of Example 1 was replaced with a nonwovenpolyester (compatible with copolyether ester polymers) fabric (obtainedfrom Freudenberg, Germany) and the resulting laminate had peel strengthvalues of 0.88 N/cm (MD) and 1.06 N/cm (CD) and an MVTR value of 750g/m²/24 hr (by method ASTM E96-B).

Example 3

A composition was prepared by dry blending 70% by weight of acopolyether ester thermoplastic elastomer (Hytrel® 8206 obtained fromDuPont) with 4% by weight UV stabilizer (Hytrel® 20UV), 4% by weightheat stabilizer (Hytrel® 30HS), 8% by weight of a maleic anhydridemodified polyolefin copolymer (Fusabond® 373) and 14% by weight of apolypropylene polymer resin (PF331 obtained from Montell Polyolefins,Wilmington, Del.). The blend was extruded under the same conditions asdescribed in Example 1 and melt laminated to the same Typar® nonwovenfabric described in Comparative Example 2. The resulting laminate had acoating thickness of about 25 microns and peel strength values of 0.26N/cm (MD) and 0.18 g/cm (CD) and an MVTR of 800 g/m²/24 hr (by methodASTM E96-B).

Example 4

A composition was prepared by dry blending 80% by weight of acopolyether ester thermoplastic elastomer (Hytrel® 8206) with 9.3% byweight polypropylene resin (PF331 obtained from Montell Polyolefins,Wilmington, Del.), 4.7% by weight PE-LLD (Novapol 8111) obtained fromNovacor Chemicals Inc., Leominster, Mass.), 4.7% by weight of a HDPEcontaining 30% by weight of 1 micron particle size CaCO₃ (Zemid™ 610obtained from DuPont Canada, Mississauga, Ontario) and 1.3% by weight ofa maleic anhydride modified polyolefin copolymer (Fusabond® MD353D).Zemid™ is a trademark of DuPont Canada. The blend was extruded under thesame conditions as described in Example 1 at a line speed of 14 m/minand melt laminated to a corona treated, spunbonded, HDPE nonwoven fabricmade by Corovin GMBH, of Peine, Germany. The resulting laminate had acoating thickness of about 31 microns, a peel strength of 0.64 N/cm, atensile strength of 9.1 N/cm (MD) and 3.6 N/cm (CD), and an MVTR of 907g/m²/24 hr (by method ASTM E96-B).

Example 5

Example 4 was repeated at a line speed of 23 m/min., resulting inlaminate that had a coating thickness of about 20 microns and peelstrength 0.18 N/cm and an MVTR of 1011 g/m²/24 hr (by method ASTME96-B).

Example 6

A composition was prepared by dry blending 50% by weight of acopolyether ester thermoplastic elastomer (Hytrel® 8206) with 33% byweight of another copolyether ester thermoplastic elastomer (Hytrel®G3548W obtained from DuPont), 8.0% by weight polypropylene (PF331), 2.6%by weight PE-LLD (Novapol 8111), 5.4% by weight of a HDPE containing 30%by weight of 1 micron particle size CaCO₃ (Zemid™ 610) and 1.0% byweight of a maleic anhydride modified polyolefin copolymer (Fusabond®MD353D). The blend was extruded under the same conditions as describedin Example 1 at a line speed of about 24 m/min and was melt laminated tothe HDPE nonwoven fabric used in Example 4. The resulting laminate had acoating thickness of about 20 microns and peel strength values of 0.09N/cm and an MVTR of 1159 g/m²/24 hr (by method ASTM E96-B).

Example 7

A composition was prepared by dry blending 50% by weight of acopolyether ester thermoplastic elastomer (Hytrel® 8206) with 31% byweight of another copolyether ester thermoplastic elastomer (Hytrel®8171 obtained from DuPont), 8.9% by weight polypropylene (Fina 3365obtained from Fina Oil and Chemical of Dallas, Tex.), 2.9% by weightPE-LLD (Novapol 8111), 6.1% by weight of 1 micron particle size CaCO₃(Zemid™ 610), and 1.1% by weight of a maleic anhydride modifiedpolyolefin copolymer (Fusabond® MD353D). The blend was extruded onto acorona treated, spunbonded, polyethylene nonwoven fabric made byPolybond of Waynesboro, Va. and adhered to the nonwoven via a vacuumprocess. The resulting laminate had a coating thickness of about 15microns and a peel strength of 0.05 N/cm and an MVTR of 1409 μm²/24 hr(by method ASTM E96-B).

Examples 8-17

The film compositions described below were prepared by dry blending twocopolyether ester thermoplastic elastomers, either an anhydride modifiedpolypropylene or an anhydride modified ethylene vinyl acetate, andtitanium dioxide. The individual components in the film compositionswere as follows:

Hytrel® 8206 copolyether ester thermoplastic elastomer sold by DuPont,and having a melting point of 200° C., a vicat softening temperature of151° C., and a shore hardness of 45D.

Hytrel® 8171 copolyether ester thermoplastic elastomer sold by DuPont,and having a melting point of 150° C., a vicat softening temperature of76° C., and a shore hardness of 32D.

Bynel® 50E561 anhydride modified polypropylene sold by DuPont, andhaving a melting temperature of 141° C., and a vicat softeningtemperature of 109° C.

Bynel® 50E555 anhydride modified polypropylene sold by DuPont, andhaving a melting temperature of 166° C., and a vicat softeningtemperature of 144° C.

Bynel® 3860 anhydride modified ethylene vinyl acetate sold by DuPont,and having a melting temperature of 74° C., and a vicat softeningtemperature of 48° C.

TiO₂ Concentrate was a concentrate of 50% by weight particulate titaniumdioxide pigment in high density polyethylene.

The film compositions used in Examples 8-17 had the followingcompositions:

Film Composition A B C D E Hytrel ® 8206 49% 49% 40% 41% 34% Hytrel ®8171 32% 32% 40% 43% 50% Bynel ® 50E561 13% — — — — Bynel ® 50E555 — 13%14% — — Bynel ® 3860 — — — 10% 10% TiO₂ Concentrate  6%  6%  6%  6%  6%

The compositions were each fed to a melt extrusion coating lineincluding a single screw extruder with an attached mixing head. Thescrew extruder was made by Egan Division of Davis-Standard Corporation.The compositions were fed to the extruder where they reached atemperature of about 263° C. and a pressure of 3827 kPa. The melts werefed to a film die with a width of about 80 cm that was maintained atabout 220° C.

The melted polymer compositions were laminated onto sheets of cardedpolypropylene staple fiber, with fiber lengths generally ranging between2.5 cm and 7.5 cm, that had been airlayed and thermal bonded. Thepolypropylene fiber sheet had a basis weight of 0.0305 kg/m² (0.9oz/yd²), a tensile strength of 8.3 N/cm (4.73 lb/in) in the machinedirection and 1.5 N/cm (0.86 lb/in) in the cross direction, and anelongation of 73% in the machine direction and 95% in the crossdirection. The polypropylene fiber sheet was spaced 24.1 cm (9.5 in)from the opening of the die and the sheet moved at a line speed of 32m/min during lamination. The polymer melt and polypropylene fiber sheetwere passed through a pair of nip rolls (one metal faced roll againstthe fibrous sheet material and one rubber faced roll against the polymermelt). The metal roll was maintained at about 43.3° C. (110° F.) bywater cooling. Air cylinders at a pressure of 414 kPa (60 psi) were usedto press the rolls together. The resulting composite sheets had theproperties set forth in Table 1 below.

TABLE I Example 8 9 10 11 12 13 14 15 16 17 Film A A B B C C D D E EComposition Film Thickness 20 25 20 25 20 25 20 25 20 25 (micron)Composite 165 183 173 170 170 160 155 155 150 160 Thickness (mm) MVTR3418 3051 3486 3536 3651 3346 4246 3489 3444 3255 (Desiccant Method)(g/m²/day) Dynamic 0.36 0.31 0.28 0.37 0.16 0.04 0.12 0 0 0 Impact (g/m²@ 2400 J/m²) Peel Strength 0.41 0.73 0.34 0.59 0.47 0.38 0.47 full* 0.27full* MD (N/cm) CD 0.33 0.53 0.36 0.39 0.29 0.43 0.57 0.37 0.41 0.66Tensile Strength (N/cm) MD 11.7 13.7 11.4 11.7 13.1 14.4 10.2 9.8 10.511.7 CD 2.5 2.3 2.3 2.5 1.8 2.1 1.8 2.1 1.8 1.9 Elongation (%) MD 61 6688 80 67 60 60 80 65 66 CD 103 106 104 81 106 67 108 96 107 109 PinholeNone None None None None None None None None None Seepage Gurley HillAir >3600 >3600 — — >3600 >3600 — — >3600 >3600 Porosity (sec) *fullbond had peel strength > 0.75 N/cm

Examples 18-31

Examples 18-31 were conducted to determine the effect of various processconditions on composite sheet properties. Examples 18-30 do not attemptto optimize end product properties. A film composition was prepared bydry blending 50% Hytrel® 8206, 33% by weight Hytrel® 8171, 4% by weightof another copolyether ester thermoplastic elastomer (Hytrel® 4056 soldby DuPont; melting temperature 150° C., vicat softening temperature 108°C., and a shore hardness of 40D) containing 50% by weight Ti-Pure® R960titanium dioxide, and 13% by weight Bynel® 50E561. Ti-Pure® is aregistered trademark of DuPont. The composition was fed to a meltextrusion coating line including a single screw extruder running at 20rpm with a helical screw configuration. The zones of the extruder wereheated to the temperature set forth in Table 2. The molten polymermixture was fed to a film die with a width of about 35 cm that wasmaintained at same temperature as the extruder. The blend was extrudedunder the conditions set forth in Table 2, below, onto a moving fibroussheet. The film composition joined the fiber sheet at a nip, as shown inFIG. 3, that was spaced about 9 cm (3.5 in) from the opening of the die.

The fibrous sheet was either a carded nonwoven (“C”) or a spunbondednonwoven (“S”). The carded sheet was made of carded polypropylene staplefiber, with fiber lengths generally ranging between 2.5 cm and 7.5 cm,that had been airlayed and thermal bonded. The polypropylene fiber sheethad a basis weight of 0.0305 kg/m² (0.9 oz/yd²), a tensile strength of8.3 N/cm (4.73 lb/in) in the machine direction and 1.5 N/cm (0.86 lb/in)in the cross direction, and an elongation of 73% in the machinedirection and 95% in the cross direction. The spunbonded sheet was aspunbonded polypropylene with a basis weight of 0.0288 kg/m² (0.85oz/yd²), a tensile strength of 11.4 N/cm (6.5 lb/in) in the machinedirection and 2.5 N/cm (1.4 lb/in) in the cross direction, and anelongation of 92% in the machine direction and 93% in the crossdirection. In the Examples in Tables 2 and 3 for which “coronatreatment” is indicated, before the fibrous sheet and the moisture vaporpermeable film are joined, the fibrous sheet was passed at a sheet speedof 15 m/min through a Model RX-8 Corona Surface Treater manufactured byENI Power Systems, Inc., that was set at a frequency of 25 kHz, and apower of 500-600 Watts.

Processing parameters were controlled to determine how changingindividual processing conditions impacted the sheet properties of peelstrength, moisture vapor transmission, and dynamic barrier.

Examples 18-21 together demonstrate how increasing the temperature ofthe rolls 34 and 36 improve the peel strength of the composite sheet.

Examples 18, 22 and 23 together demonstrate how increasing thetemperature of the die 38 through which the film composition is extrudedimprove the peel strength of the composite sheet.

Examples 24-26 together show how increasing the film thickness byslowing the line speed improves the peel strength of the compositesheet.

Examples 25 and 27 together demonstrate how the use of a more fibrouscarded sheet material improves the peel strength of the composite sheet.

Examples 28, 29 and 30 show how increasing the temperature of the niprolls 34 and 36 (FIG. 3) improves peel strength of the sheet, but alsoreduces moisture vapor transmission through the composite sheet.Differential Scanning Calorimetry measurements of the heat of fusionsuggest that at the lower roll temperatures of Example 28, the filmmorphology is more amorphous, as compared to a more crystalline filmmorphology generated at the higher roll temperatures of Example 30.Thus, it appears that a more amorphous film morphology generated withlower roll temperatures results in a higher moisture vapor transmissionrate.

Examples 25 and 31 show how increasing the pressure applied against thenip rolls 34 and 36 improves the peel strength of the sheet. In Example31, a 138 kPa (20 psi) pressure was used in the pneumatic system topress roll 34 against roll 36. In Example 25, all processing conditionswere the same as in Example 31 except that the pressure was 550 kPa (80psi), as was also applied in Examples 18-30, such that the nip force inExample 25 was significantly greater than the nip force in Example 31.The increased nip force resulted in an increase in peel strength.

TABLE 2 Example 18 19 20 21 22 23 24 Roll Temperature 40 15 76 115 42 4240 at Nip (° C.) Extruder and 220 220 220 220 240 260 220 DieTemperature (° C.) Line Speed 13 13 13  13 13 13 18 (m/min) Substrate CC C C C C C Composition Corona Treated Yes Yes Yes Yes Yes Yes No FilmThickness 22 22 22 ~22 26 ~22 16 (micron) Peel Strength 0.06 0.04 0.25Full 0.27 Full 0.01 (N/cm) MVTR 2700 2600 2400 2600  2400 2300 3100(g/m²/24 hr) Dynamic Impact 0.0 0.0 0.0   87* 0.01 1.34* 0.07 (g/m² @2400 J/m²) Roll Temperature 40 40 40  10 40 60 40 at Nip (° C.) (138 kPapressure) Roll Temperature 40 40 40  10 40 60 40 at Nip (° C.) (138 kPapressure) Extruder and 220 220 220 220 220 220 220 Die Temperature (°C.) Example 25 26 27 28 29 30 31 Line Speed 13 10 13  13 13 13 13(m/min) Substrate C C S C C C C Composition Corona Treated No No No YesYes Yes No Film Thickness 23 29 21  22 30 28 22 (micron) Peel Strength0.07 0.23 0.03   0^(#) 0.23 0.61 0.04 (N/cm) MVTR 2600 2400 2800 2800 2700 2500 2800 (g/m²/24 hr) Dynamic Impact 0.0 0.13 0.1    0.03 — 0.280.08 (g/m² @ 2400 J/m²) no hold/10 sec hold *pinholes present due toexcessive bonding ^(#)Had sticking to small roll, may have reduced peel.

Examples 32-34

A film composition was prepared by dry blending 57.5% by weight of acopolyether ester thermoplastic elastomer (Hytrel® 8206), 38% by weightof another copolyether ester thermoplastic elastomer (Hytrel® 8171), and4.5% by weight of another copolyether ester thermoplastic elastomer(Hytrel® 4056) containing 50% by weight Ti-Pure® R960 titanium dioxidepigment. The composition was fed to a melt extrusion coating lineincluding a single screw extruder running at 20 rpm with a helical screwconfiguration. The heating zones of the extruder were set to 220° C. Themolten polymer mixture was fed to a film die with a width of about 35 cmthat was maintained at 220°. The blend was extruded under the conditionsset forth in Table 3, below, onto a moving fibrous sheet. The filmcomposition joined the fiber sheet at a nip, as shown in FIG. 3, thatwas spaced about 9 cm (3.5 in) from the opening of the die.

The fibrous sheet was a carded nonwoven (“C”) made of cardedpolypropylene staple fiber, with fiber lengths generally ranging between2.5 cm and 7.5 cm, that had been airlayed and thermal bonded. Thepolypropylene fiber sheet had a basis weight of 0.0305 kg/m² (0.9oz/yd²), a tensile strength of 8.3 N/cm (4.73 lb/in) in the machinedirection and 1.5 N/cm (0.86 lb/in) in the cross direction, and anelongation of 73% in the machine direction and 95% in the crossdirection. Processing conditions were optimized such that peel strengthsof from 0.08 to 0.29 N/cm were obtained without the addition of apolyolefin or a compatibilizer to the polyether ester polymer of themoisture permeable film layer material.

TABLE 3 Example 32 33 34 Roll Temperature at 40 40 40 Nip (° C.)Extruder and 220 220 220 Die Temperature (° C.) Line Speed (m/min) 13 1313 Substrate C C C Composition Corona Treated Yes Yes No Film Thickness31 24 25 (micron) Peel Strength 0.29 0.08 0.10 (N/cm) MVTR (g/m²/24 hr)3600 3600 3500 Dynamic Impact 0.0 0.0 0.0 (g/m² @ 2400 J/m²)

Example 35

A film composition was prepared as in Examples 19-31. The compositionwas fed to a melt extrusion coating line including a single screwextruder running at 20 rpm with a helical screw configuration. Theheating zones of the extruder were set to 220° C. The molten polymermixture was fed to a film die with a width of about 35 cm that wasmaintained at 220°. The blend was extruded under the conditions setforth below, between two moving fibrous sheets. The film compositionjoined the fiber sheets at a nip, similar to that shown in FIG. 3.However, one fibrous sheet was fed into the nip on each of the rolls 34and 36, and both fibrous sheets joined the film layer at the nip. Theopening of the nip was spaced about 9 cm (3.5 in) from the opening ofthe die.

Each of the fibrous sheets was a carded nonwoven (“C”) made of cardedpolypropylene staple fiber, with fiber lengths generally ranging between2.5 cm and 7.5 cm, that had been airlayed and thermal bonded. Thepolypropylene fiber sheet had a basis weight of 0.0305 kg/m² (0.9oz/yd²), a tensile strength of 8.3 N/cm (4.73 lb/in) in the machinedirection and 1.5 N/cm (0.86 lb/in) in the cross direction, and anelongation of 73% in the machine direction and 95% in the crossdirection. The composite sheet formed was like that shown in FIG. 2.Processing conditions and product properties are listed on Table 4below.

TABLE 4 Example 35 Roll Temperature at 70 Nip (° C.) Extruder and 220Die Temperature (° C.) Line Speed (m/min) 13 Substrate C Composition(both sheets) Corona Treated Yes Film Thickness 24 (micron) PeelStrength 0.11 (N/cm) (side A) 0.16 (side B) MVTR (g/m²/24 hr) 2300Dynamic Impact 0.10 (g/m² @ 2400 J/m²)

Examples 36-39

A first polymer composition was prepared as in Examples 19-31. Thisfirst polymer composition was fed to a 38 mm diameter extruder at atemperature of 220° C. which was run at 20 rpm. The output of this 38 mmextruder was connected to a melt combining block. A second polymercomposition comprised of 100% Hytrel® 4778 (melting point 208° C., vicatsoftening temperature 175° C., and Shore hardness of 47D) was fed to a25 mm diameter extruder that was also connected to the same meltcombining block. This 25 mm diameter extruder was also operated at atemperature of 220° C. In Examples 36-39, the speed of the 25 mmextruder was varied from 20 rpm to 1.5 rpm to generate films wherein thethickness of the layer of the second polymer composition varied. Thecoextruded layers were combined in the melt combining block. The layerswere then passed through a die that was connected to the combiningblock. The die had a 35 cm wide die block that was heated to about 220°C.

A bonded bicomponent film was formed and exited the die. The layer ofthe first polymer composition maintained a nominal thickness of about 22microns in each of the Examples 36-39. The thickness of the layers ofthe second polymer composition was between 4 and 0.2 microns. This filmwas bonded with a hot melt adhesive in a spiral spray pattern to apolyethylene 30.5 micron (1.2 mil) film (from Tredegar Film Products) ofthe type used in backsheets of absorbent articles. The hot melt adhesivewas a linear SIS adhesive (Findley H2031) of the type that is currentlybeing used in diaper manufacturing.

To measure the “construction peel strength” of the resulting bondbetween the polyethylene film and the second polymer composition, 1 inchwide strips of the two materials were prepared and facially bonded toone another over an area measuring one square inch, leaving an opposedpair of unbonded flaps on at least one end of the strips long enough tospan the gage length of the testing unit. The adhesive utilized was alinear SIS adhesive commercially available from Findley Adhesives underthe designation H2031, applied at a 0.009 grams/square inch add-on levelin a spiral spray pattern. Three samples were prepared for each testsequence, with the reported results comprising an average of the resultsfor the three samples. An Instron table model tester was utilized with a5 pound load cell, a 2 inch gage length, and a crosshead speed of 20inches per minute, in a manner generally consistent with the Elongationto Break test described above. Opposing unbonded flaps of the twomaterials were clamped in the respective clamps of the tester, with thesecond polymer composition in the upper clamp. Specimens were evaluatedat the point of failure when delamination of the adhesive bond or thesubstrates themselves occurred.

Bicomponent film/polyethylene constructions were prepared according tothe following conditions to obtain the following properties:

TABLE 5 Example 36 37 38 39 Extruder Speed (rpm) 20 10 5 1.5 (25 mmextruder) Thickness-second film 4 1.7 0.7 0.2 layer (microns)MVTR-bicomponent 2700 2800 2900 2900 film (g/m²/day) Construction peel2.47 1.71 1.70 1.43 strength - Dry (N/cm) Construction peel 1.78 1.931.73 1.63 strength - Wet* (N/cm) *Wet state means test sample was soakedin distilled water for 30 minutes.

Comparative Example 1

A sample of Exxon Exxair XFB-100W microporous film, available from ExxonChemical Company of Buffalo Grove, Ill., USA, was tested for moisturevapor transmission rate, dynamic fluid transmission, microbial barrierfor sterile packaging, and liquid moisture seepage. The propertiesmeasured were as follows:

MVTR (g/m²/24 hr) 4000 Dynamic Impact   0.97 (g/m² @ 2400 J/m²)Microbial Barrier Bacillus subtilis bacteria passage recorded in six ofsix samples tested after 15 minute exposure. (38.6 cm Hg vacuum; 2.8l/min flow rate) Moisture Seepage Dye apparent on blotter indicatingpassage of liquid.

It will be apparent to those skilled in the art that modifications andvariations can be made in breathable composite sheet material of thisinvention. The invention in its broader aspects is, therefore, notlimited to the specific details or the illustrative examples describedabove. Thus, it is intended that all matter contained in the foregoingdescription, drawings and examples shall be interpreted as illustrativeand not in a limiting sense.

1. A moisture vapor permeable, substantially liquid impermeablecomposite sheet material comprising a fibrous substrate and a moisturevapor permeable thermoplastic film layer; said fibrous substratecomprised of synthetic fibers, said synthetic fibers being comprised ofat least 50% by weight polyolefin polymer, said substrate havingopposite first and second planar sides; said moisture vapor permeablefilm layer comprised of at least about 50% by weight of polymer selectedfrom the group of block copolyether esters, block copolyether amides,polyurethanes, and combinations thereof, said film layer being meltbonded directly to the first side of said substrate in the absence of anadhesive between the film layer and the substrate; and said compositesheet exhibiting a peel strength of at least 0.1 N/cm, a dynamic fluidtransmission of less than about 0.75 g/m² when subjected to an impactenergy of about 2400 joules/m², and having a moisture vapor transmissionrate, according to the desiccant method, of at least 1500 g/m²/24 hr. 2.The composite sheet of claim 1 wherein the film layer has an averagethickness of less than about 50 microns.
 3. The composite sheet of claim1 wherein said composite sheet has a peel strength of at least about0.15 N/cm.
 4. The composite sheet of claim 3 wherein said compositesheet has a peel strength per unit thickness of the film layer of thesheet material of at least 0.003 N/cm-micron.
 5. The composite sheet ofclaim 3 wherein the film layer of said composite sheet has a thicknessof less than 30 microns, and the composite sheet has a moisture vaportransmission rate, according to the dessicant method, of at least 2500g/m²/24 hr.
 6. The composite sheet of claim 5 wherein said film layer ofsaid composite sheet has a thickness between about 10 microns and about25 microns, and the basis weight of said fibrous substrate is betweenabout of 13.5 and about 40 g/m².
 7. The composite sheet of claim 2wherein the film layer has opposite first and second sides, said firstside being melt bonded directly to the first side of said substrate, andwherein said first side of said film layer has a surface area per unitarea that is greater than the surface area per unit area of said secondside of said film layer.
 8. The composite sheet of claim 1 wherein saidsheet has a dynamic fluid transmission of less than about 0.5 g/m² whensubjected to an impact energy of about 2400 joules/m².
 9. The compositesheet of claim 8 wherein the composite sheet is substantially free ofmicropores, and substantially no liquid moisture passes through thesheet when tested according to the liquid moisture seepage test.
 10. Thecomposite sheet of claim 8 wherein said composite sheet prevents passageof microbes when tested according to the ISO 11607 standard for sterilepackaging materials.
 11. The composite sheet of claim 1 wherein saidcomposite sheet has a machine direction tensile strength and a crossdirection tensile strength of at least about 1 N/cm, and a machinedirection elongation and a cross direction elongation of at least about30%.
 12. The composite sheet of claim 11 wherein said fibrous substrateconsists essentially of fibers of polyolefin polymer.
 13. The compositesheet of claim 1 wherein said film layer comprises a moisture vaporpermeable film having multiple layers, each of such multiple layersbeing comprised of a different moisture vapor permeable thermoplasticpolymer composition.
 14. The composite sheet of claim 13 wherein one ofsaid film layers comprises a substantially hydropbilic film layer andone of said film layers comprises a substantially hydrophobic filmlayer.
 15. The composite sheet of claim 1, wherein said composite sheetfurther includes an additional layer of diverse construction andcomposition from said film layer and said fibrous substrate.
 16. Thecomposite sheet of claim 15, wherein said additional layer comprises amicroporous film.
 17. The composite sheet of claim 1 wherein said filmlayer is comprised at least 50% by weight of a Fraction A consistingessentially of polymer from the group of block copolyether esters, blockcopolyether amides, polyurethanes and combinations thereof, at least 5%by weight of a Fraction B consisting essentially of a polymer from thegroup of homopolymers of an alpha-olefin, copolymers or terpolymerscontaining an alpha-olefin and one or more other monomers, and blockcopolymers of a vinylarene and a conjugated diene, and at least 0.1% byweight of a Fraction C consisting essentially of a compatibilizer forFractions A and B.
 18. The composite sheet material of claim 17 whereinfilm Fraction C consists essentially of homopolymers, copolymers andterpolymers with backbones that are compatible with Fraction B, saidbackbones being grafted with a monomer having a functional group that iscompatible with Fraction A.
 19. The composite sheet material of claim 18wherein film Fraction C is a polymer with a backbone identical toFraction B, said backbone being grafled with monomer selected from thegroup of alpha- and beta-ethylenically unsaturated carbonic acids andanhydrides, and derivatives thereof.
 20. The composite sheet material ofclaim 19 wherein the film layer comprises, by weight, 50% to 95% filmFraction A, 5% to 40% film Fraction B, and 0.1% to 15% film Fraction C.21. The composite sheet material of claim 20 wherein film Fraction A isa block copolyether ester, film Fraction B is polypropylene, filmFraction C is a grafted polymer having a backbone of polypropylene thatis grafted with maleic anhydride, and the substrate is a carded fibrousweb comprised of at least 75% by weight polypropylene.